11 research outputs found
UZM-8 Zeolite Synthesized from Solid Aluminosilicate Gel and Its Catalytic Performance
Instead of conventional aluminum isopropoxide and silica sources, commercially available solid aluminosilicate gel with SiO2/Al2O3 = 25 was selected to synthesize UZM-8 zeolite with diethyl-dimethylammonium hydroxide (DEDMAOH) as the structure-directing agent (SDA) in the Na+-free system. The structure-directing function and decomposition of DEDMAOH were analyzed. With the irregular stacking of MWW layers, UZM-8 zeolite with solid aluminosilicate gel as silica and aluminum sources possessed better stability during crystallization, better crystallinity, higher surface area, clearly separated Si-29 MAS NMR resonances, and more acid sites accessed by pyridine and 2,4,6-trimethyl-pyridine than conventional synthesized UZM-8 zeolite, which resulted in obvious improvement in ethylene conversion with little loss in ethylbenzene selectivity at higher temperatures
A newly designed chamber for the acclimatization of coconut plantlets coming from in vitro
Green Production Technology of the Monomer of Nylon-6: Caprolactam
After two decades’ endeavor, the Research Institute of Petroleum Processing (RIPP) has successfully developed a green caprolactam (CPL) production technology. This technology is based on the integration of titanium silicate (TS)-1 zeolite with the slurry-bed reactor for the ammoximation of cyclohexanone, the integration of silicalite-1 zeolite with the moving-bed reactor for the gas-phase rearrangement of cyclohexanone oxime, and the integration of an amorphous nickel (Ni) catalyst with the magnetically stabilized bed reactor for the purification of caprolactam. The world’s first industrial plant based on this green CPL production technology has been built and possesses a capacity of 200 kt·a−1. Compared with existing technologies, the plant investment is pronouncedly reduced, and the nitrogen (N) atom utilization is drastically improved. The waste emission is reduced significantly; for example, no ammonium sulfate byproduct is produced. As a result, the price difference between CPL and benzene drops. In 2015, the capacity of the green CPL production technology reached 3 × 106 t·a−1, making China the world’s largest CPL producer, with a global market share exceeding 50%
Transformation from NaA to MCM-49 Zeolite and Its Catalytic Alkylation Performance
The transformation from NaA (LTA)
to MCM-49 (MWW) zeolite was achieved
in the synergism of hexamethyleneimine (HMI), NaOH, and SiO<sub>2</sub>, in spite of no common composite build units between LTA (<i>lta</i>, <i>sod</i>, and <i>d4r</i>) and
MWW (<i>mel</i> and <i>d6r</i>) structure. NaA
(SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> = 2.0) was employed as
the parent zeolite. The samples prepared at different crystallization
stages were characterized by XRD, SEM, <sup>29</sup>Si/<sup>27</sup>Al/<sup>13</sup>C MAS NMR, and STEM-EDS to investigate the intermediates
during the transformation from NaA to MCM-49. As shown in SEM and
STEM-EDS images, MCM-49 was proposed to be transformed gradually from
the exterior to the interior of NaA, which was clearly observed by
the core (LTA, low SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub>)–shell
(MWW, high SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub>) coexisting
zeolites as intermediates. With high relative crystallinity and the
uniform sizes of crystals, the final MCM-49 was featured by Si enrichment
on the external surface, which was proved by the shell (SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> = 45.4) wrapping around the core (SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> = 22.0). For transformed H-MCM-49
zeolite, the uniform sizes of crystals and the increase of total acid
sites contributed to better accessibility of active centers, which
achieved simultaneous improvement in ethylene conversion and ethylbenzene
selectivity in the liquid-phase alkylation of benzene with ethylene