Previous Page  10 / 13 Next Page
Information
Show Menu
Previous Page 10 / 13 Next Page
Page Background

Page 45

conferenceseries

.com

Volume 08

Research & Reviews: Journal of Engineering and Technology

ISSN: 2319-9873

Automobile Europe 2019

July 08-09, 2019

6

th

International Conference and Exhibition on

July 08-09, 2019 | Zurich, Switzerland

Automobile & Mechanical Engineering

Comparison of hydrocaron components affecting de-nox performance of hc-selective catalytic reduction

catalysts

Kyungseok Lee

1

, Hidenori Kosaka

1

, Susumu Sato

1

, Toshiyuki yokoi

1

and

Byungchul Choi

2

1

Tokyo Institue of Technology, Japan

2

Chonnam National University, South Korea

T

he catalytic performance of copper (Cu)-containing zeolite catalysts supported on various types of zeolites

(chabaziete, MFI, and BEA frameworks) was investigated in the hydrocarbon (HC)-selective catalytic reduction

(SCR) of NOx with C

3

H

6

and n-C

4

H

10

as reducing agents. The catalysts were prepared by an wetness incipient

impregantion method with varying copper loadings from 1 to 10 wt%, thereafter they were washcoated on the

commericial monolitic honeycomb substrate. All the prepared powder catalytst were characterized by N

2

adsorption

isotherms, powder X-ray diffraction (XRD), inductively coupled plasma–atomic emission spectrometry, solid-

state

27

Al magic angle spinning–nuclear magnetic resonance, ultraviolet–visible spectroscopy, X-ray photoelectron

spectroscopy, field emission scanning electron microscopy, and high-resolution scanning electron microscopy. The

impregnation of Cu to the respective zeolites did not modify the inherent zeolite topology, whereas the loading levels

of copper and zeolite topology significantly affected the de-NOx performance of Cu/zeolites. Among the Cu/zeolite

catalysts, 2Cu/ZSM-5 showed the best catalytic performance both the C3H6- and C

4

H

10

-SCR, exhibiting a nearly

70% de-NOx performance at 360

0

C in C

3

H

6

-SCR and 74% NOx conversion at 450-465

0

C in C

4

H

10

-SCR, followed

by Cu/BETA and Cu/SSZ-13. The effects of coexistent gases (0-8 vol.% oxygen and 0-10 vol.% carbon dioxide) and

hydrothermal aging at 700

0

C were also evaluated. Oxygen was an indispensable component for the HC-SCR process,

and its concentration affected the N

2

selectivity and temperature window of the maximum de-NOx performance.

The presence of CO

2

in the feed stream was an inhibitor for NOx reduction.

lee.k.aj@m.titech.ac.jp

JET 2019, Volume 08