Abstract: A multi-layer full dense mesh (MFDM) device. The MFDM may include a metal-top layer including a bump pad array that may include a power1 (PWR1) bump pad within a PWR1 bump region, a VSS bump pad within a VSS bump region, and a power2 (PWR2) bump pad within a PWR2 bump region. The metal-top layer may also include a PWR1 majority metal-top region. The MFDM may also include a metal-top-1 layer beneath the metal-top layer and including a VSS majority metal-top-1 region, a PWR1 metal-top-1 region, and a PWR2 metal-top-1 region. The MFDM may also include a metal-top-2 layer beneath the metal-top-1 layer and including a PWR2 majority metal-top-2 region, a VSS metal-top-2 region, and a PWR1 metal-top-2 region. The MFDM may also include top-1 VIAs disposed between the metal-top layer and the metal-top-1 layer, and top-2 VIAs disposed between the metal-top-1 layer and the metal-top-2 layer.

Abstract: A multi-layer full dense mesh (MFDM) device. The MFDM may include a metal-top layer including a bump pad array that may include a power1 (PWR1) bump pad within a PWR1 bump region, a VSS bump pad within a VSS bump region, and a power2 (PWR2) bump pad within a PWR2 bump region. The metal-top layer may also include a PWR1 majority metal-top region. The MFDM may also include a metal-top-1 layer beneath the metal-top layer and including a VSS majority metal-top-1 region, a PWR1 metal-top-1 region, and a PWR2 metal-top-1 region. The MFDM may also include a metal-top-2 layer beneath the metal-top-1 layer and including a PWR2 majority metal-top-2 region, a VSS metal-top-2 region, and a PWR1 metal-top-2 region. The MFDM may also include top-1 VIAs disposed between the metal-top layer and the metal-top-1 layer, and top-2 VIAs disposed between the metal-top-1 layer and the metal-top-2 layer.

Abstract: Novel catalytic compositions for cracking of crude oil fractions are disclosed. The catalytic compositions comprise a basic material. When used in a cracking process, preferably a FCC process, the resulting LCO and HCO fractions have desirably low aromatics levels. Further disclosed is a one-stage FCC process using the catalytic composition of the invention. Also disclosed is a two-stage FCC process for maximizing the LCO yield.

Abstract: A particulate unsupported superacid catalyst for use in fluid catalytic cracking is provided comprising doped silica which has been doped with from about 1 to about 99 wt %, based on the weight of the catalyst composition, of at least one inorganic oxide dopant selected from the group consisting of rare earth metal oxides, alkaline earth metal oxides, zinc oxide, magnesium oxide, manganese oxide, yttrium oxide, niobium oxide, zirconium oxide and titanium oxide, and wherein the doped silica has been anion-modified by an anion selected from the group consisting of phosphate, tungstate, and sulphate.

Abstract: Novel catalytic compositions for cracking of crude oil fractions are disclosed. The catalytic compositions comprise a basic material. When used in a cracking process, preferably a FCC process, the resulting LCO and HCO fractions have desirably low aromatics levels. Further disclosed is a one-stage FCC process using the catalytic composition of the invention. Also disclosed is a two-stage FCC process for maximizing the LCO yield.

Abstract: Processes for maximizing low aromatics LCO yield and/or propylene yield in fluid catalytic cracking are disclosed. The processes employ catalytic compositions that comprise a predominantly basic material and little to no large pore zeolite.

Abstract: Processes for maximizing low aromatics LCO yield and/or propylene yield in fluid catalytic cracking are disclosed. The processes employ catalytic compositions that comprise a predominantly basic material and little to no large pore zeolite.

Abstract: Novel catalytic compositions for cracking of crude oil fractions are disclosed. The catalytic compositions comprise a basic material and at least one intermediate and/or small pore zeolite, and comprises little to no large pore zeolite.