Provided herein is an exhaust system comprising a diesel particulate filter coated with a selective catalytic reduction (SDPF) wherein the SCR is coated with a Cu/LTA catalyst comprising a LTA zeolite that includes copper ions and the SCR is coated on a high pore diesel particulate matter filter, wherein a ratio of copper and aluminum is from about 0.14 to about 0.48, and wherein the Si/Al ratio of the LTA zeolite is from about 8 to about 100.

A catalyst according to an example embodiment includes an LTA zeolite having copper ions, wherein the weight ratio of copper to aluminum is from about 0.14 to about 0.58, and the weight ratio of silicon to aluminum of the LTA zeolite exceeds 1.

There is provided a zeolite which has excellent NOx purifying performance, particularly excellent NOx purifying performance after heat endurance. The zeolite has a CHA structure in which Cu and Ce are carried, and has a Cu/Al molar ratio of 0.25 to 0.48 and a Ce/Al molar ratio of 0.01 to 0.03.

Provided are a novel synthesis technique for producing a metal promoted aluminosilicate zeolite have a small pore framework and methods of using the same.

The present disclosure is directed to processing for preparing crystalline pure-silica and heteroatom-substituted LTA frameworks in fluoride media using a simple organic structure-directing agent (OSDA), having a structure of Formula (I):

##STR00001##

where substituents R.sup.1 to R.sup.9 are defined herein. Aluminosilicate LTA is an active catalyst for the methanol to olefins reaction with higher product selectivities to butenes as well as C5 and C6 products than the commercialized catalysts. Titanosilicate LTA is an active catalyst for the epoxidation of allyl alcohol using aqueous H.sub.2O.sub.2.

A method for preparing molecular sieves with a Linde Type A (LTA) topology structure, and molecular sieves obtained thereby are described wherein a structure directing agent comprising a triquaternary cation is contacted with a source of a first oxide of a first tetravalent element or a source of a first oxide of a trivalent element; and a source of an oxide of a pentavalent elements.

A method of synthesizing high-silica zeolites in a fluoride media using faujasite crystals as the aluminum source and quasi-siliceous seed crystals containing a small amount of germanium is described. The faujasite crystals dissolved during hydrothermal treatment, prior to the crystallization of LTA-type zeolites. High-silica zeolites of an LTA, a CHA, a *BEA and an STT-type were produced. High-silica zeolites with a Si/Al ratio (SAR) of 63 to 420 were synthesized, with the SAR related to the amount of faujasite crystals used. The aluminosilicate LTA-type zeolite products possess nearly defect-free structures, a characteristic often seen in fluoride mediated synthesis. The unit cell volumes of the high-silica LTA-type zeolites correspond to the amount of Al present in the framework. Aluminosilicate ITW-type zeolites were produced using these methods.

Described herein are zeolite bodies, in particular those having improved physical and chemical properties, methods of manufacturing the zeolite bodies, and uses of the zeolite bodies, in particular in catalysis and gas separation.

A process for the production of a zeolite body includes the steps of: forming a zeolite reaction mix having zeolite crystallites and water; removing water from the zeolite reaction mix to form a partially dried zeolite mass; extruding and/or cutting/breaking the partially dried zeolite mass to form a partially dried zeolite body; subjecting the partially dried zeolite bodies to a further processing step selected from rounding, drying and size classification; heating the partially dried zeolite bodies to temperatures greater than 400 C. to form calcined zeolite bodies; contacting the calcined zeolite bodies with water to form washed calcined zeolite bodies; contacting the washed calcined zeolite bodies with an ammonium ion containing solution so as to exchange sodium ions in the zeolite with ammonium ions to form cation-exchanged zeolite bodies; and heating the cation-exchanged zeolite bodies to temperatures greater than 200 C. to form zeolite bodies.

A method of making a molecular sieve may include: reacting a source selected from the group consisting of: a source of a tetrahedral element in the presence of a structure directing agent (SDA) selected from the group consisting of: Ar.sup.+-L-Ar, Ar.sup.+-L-Ar-L-Ar.sup.+, Ar.sup.+-L-Ar-L-NR3.sup.+, and ArAr.sup.+-L-Ar.sup.+Ar, where Ar.sup.+ is to a N-containing cationic aromatic ring, Ar is to a non-charged aromatic ring, L is a methylene chain of 3-6 carbon atoms, NR3.sup.+ is to a quaternary ammonium, and ArAr.sup.+ and Ar.sup.+Ar are a fused aromatic ring structure comprising both a N-containing cationic portion and a non-charged portion, to produce the molecular sieve.