Study of Activated Carbon Supported Nickel Catalyst for Adsorption of Phenolic Wastewater

An activated carbon with OSGs (Oxygen Surface Groups) supported nickel catalyst shows high activity and chemoselectivity for hydrogenation of a variety of substituted nitroarenes under mild reaction conditions.

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Development of residue coal fly ash supported nickel catalyst for H2 production via glycerol steam reforming

Applied Catalysis B Environmental ◽

10.1016/j.apcatb.2021.119958 ◽

2021 ◽

Vol 291 ◽

pp. 119958

Author(s):

Kang Gao ◽

Ommolbanin Alizadeh Sahraei ◽

Maria C. Iliuta

Keyword(s):

Fly Ash ◽

Nickel Catalyst ◽

Steam Reforming ◽

Coal Fly Ash ◽

H2 Production ◽

Supported Nickel Catalyst

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Hydrogenation of anthracene over active carbon-supported nickel catalyst

Catalysis Today ◽

10.1016/s0920-5861(98)00264-8 ◽

1998 ◽

Vol 45 (1-4) ◽

pp. 361-366 ◽

Cited By ~ 26

Author(s):

Z.-G Zhang ◽

K Okada ◽

M Yamamoto ◽

T Yoshida

Keyword(s):

Nickel Catalyst ◽

Active Carbon ◽

Supported Nickel Catalyst

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Effect of Modified Nanoclay Surface Supported Nickel Catalyst on Carbon Dioxide Reforming of Methane

Topics in Catalysis ◽

10.1007/s11244-020-01403-y ◽

2021 ◽

Author(s):

Juthasiri Chaisamphao ◽

Sirapassorn Kiatphuengporn ◽

Kajornsak Faungnawakij ◽

Waleeporn Donphai ◽

Metta Chareonpanich

Keyword(s):

Carbon Dioxide ◽

Nickel Catalyst ◽

Carbon Dioxide Reforming ◽

Supported Nickel Catalyst

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COD removal of phenolic wastewater by biological activated carbon-sequencing batch reactor in the presence of 2,4-DCP

Water Science & Technology ◽

10.2166/wst.2000.0511 ◽

2000 ◽

Vol 42 (5-6) ◽

pp. 171-178 ◽

Cited By ~ 3

Author(s):

S.-R. Ha ◽

L. Qishan ◽

S. Vinitnantharat

Keyword(s):

Activated Carbon ◽

Retention Time ◽

Sequencing Batch Reactor ◽

Batch Reactor ◽

Cod Removal ◽

High Loading ◽

Treatment Efficiency ◽

Biological Activated Carbon ◽

Treatment Performance ◽

Phenolic Wastewater

Treatment performance of COD in the presence of 2,4-dichlorophenol (2,4-DCP) was explored by using a biological activated carbon-sequencing batch reactor (BAC-SBR) system. Two COD levels of basic substrate were synthesized with a mixture of phenol and 2,4-dichlorophenol. Although effluent concentration was increased with reduction of sludge retention time (SRT) from 8-days to 3-days, treatment efficiency was indicated more than 90% of COD in all SRTs applied. Reactors operated with acclimated sludge could be expected to cope with quite high loading of inhibitory substances.

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