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News Article | November 29, 2016
Site: www.newsmaker.com.au

This report studies Stationary Emission Control Catalyst in Global market, especially in North America, Europe, China, Japan, Southeast Asia and India, focuses on top manufacturers in global market, with capacity, production, price, revenue and market share for each manufacturer, covering  Hitachi Zosen Corporation  Basf  Cdti Corp  Haldor Topsoe  Nikki Universal Co., Ltd.  Jgc C&C  Cormetech Inc.  Dcl International, Inc.  Porzellanfabrik Frauenthal Gmbh  Honeywell Uop  Johnson Matthey Plc  Corning Inc. Market Segment by Regions, this report splits Global into several key Regions, with production, consumption, revenue, market share and growth rate of Stationary Emission Control Catalyst in these regions, from 2011 to 2021 (forecast), like  North America  Europe  China  Japan  Southeast Asia  India  Split by product type, with production, revenue, price, market share and growth rate of each type, can be divided into  Type I  Type II  Type III  Split by application, this report focuses on consumption, market share and growth rate of Stationary Emission Control Catalyst in each application, can be divided into  Application 1  Application 2  Application 3 1 Stationary Emission Control Catalyst Market Overview  1.1 Product Overview and Scope of Stationary Emission Control Catalyst  1.2 Stationary Emission Control Catalyst Segment by Type  1.2.1 Global Production Market Share of Stationary Emission Control Catalyst by Type in 2015  1.2.2 Type I  1.2.3 Type II  1.2.4 Type III  1.3 Stationary Emission Control Catalyst Segment by Application  1.3.1 Stationary Emission Control Catalyst Consumption Market Share by Application in 2015  1.3.2 Application 1  1.3.3 Application 2  1.3.4 Application 3  1.4 Stationary Emission Control Catalyst Market by Region  1.4.1 North America Status and Prospect (2011-2021)  1.4.2 Europe Status and Prospect (2011-2021)  1.4.3 China Status and Prospect (2011-2021)  1.4.4 Japan Status and Prospect (2011-2021)  1.4.5 Southeast Asia Status and Prospect (2011-2021)  1.4.6 India Status and Prospect (2011-2021)  1.5 Global Market Size (Value) of Stationary Emission Control Catalyst (2011-2021) 2 Global Stationary Emission Control Catalyst Market Competition by Manufacturers  2.1 Global Stationary Emission Control Catalyst Capacity, Production and Share by Manufacturers (2015 and 2016)  2.2 Global Stationary Emission Control Catalyst Revenue and Share by Manufacturers (2015 and 2016)  2.3 Global Stationary Emission Control Catalyst Average Price by Manufacturers (2015 and 2016)  2.4 Manufacturers Stationary Emission Control Catalyst Manufacturing Base Distribution, Sales Area and Product Type  2.5 Stationary Emission Control Catalyst Market Competitive Situation and Trends  2.5.1 Stationary Emission Control Catalyst Market Concentration Rate  2.5.2 Stationary Emission Control Catalyst Market Share of Top 3 and Top 5 Manufacturers  2.5.3 Mergers & Acquisitions, Expansion 3 Global Stationary Emission Control Catalyst Capacity, Production, Revenue (Value) by Region (2011-2016)  3.1 Global Stationary Emission Control Catalyst Capacity and Market Share by Region (2011-2016)  3.2 Global Stationary Emission Control Catalyst Production and Market Share by Region (2011-2016)  3.3 Global Stationary Emission Control Catalyst Revenue (Value) and Market Share by Region (2011-2016)  3.4 Global Stationary Emission Control Catalyst Capacity, Production, Revenue, Price and Gross Margin (2011-2016)  3.5 North America Stationary Emission Control Catalyst Capacity, Production, Revenue, Price and Gross Margin (2011-2016)  3.6 Europe Stationary Emission Control Catalyst Capacity, Production, Revenue, Price and Gross Margin (2011-2016)  3.7 China Stationary Emission Control Catalyst Capacity, Production, Revenue, Price and Gross Margin (2011-2016)  3.8 Japan Stationary Emission Control Catalyst Capacity, Production, Revenue, Price and Gross Margin (2011-2016)  3.9 Southeast Asia Stationary Emission Control Catalyst Capacity, Production, Revenue, Price and Gross Margin (2011-2016)  3.10 India Stationary Emission Control Catalyst Capacity, Production, Revenue, Price and Gross Margin (2011-2016) 4 Global Stationary Emission Control Catalyst Supply (Production), Consumption, Export, Import by Regions (2011-2016)  4.1 Global Stationary Emission Control Catalyst Consumption by Regions (2011-2016)  4.2 North America Stationary Emission Control Catalyst Production, Consumption, Export, Import by Regions (2011-2016)  4.3 Europe Stationary Emission Control Catalyst Production, Consumption, Export, Import by Regions (2011-2016)  4.4 China Stationary Emission Control Catalyst Production, Consumption, Export, Import by Regions (2011-2016)  4.5 Japan Stationary Emission Control Catalyst Production, Consumption, Export, Import by Regions (2011-2016)  4.6 Southeast Asia Stationary Emission Control Catalyst Production, Consumption, Export, Import by Regions (2011-2016)  4.7 India Stationary Emission Control Catalyst Production, Consumption, Export, Import by Regions (2011-2016) 5 Global Stationary Emission Control Catalyst Production, Revenue (Value), Price Trend by Type  5.1 Global Stationary Emission Control Catalyst Production and Market Share by Type (2011-2016)  5.2 Global Stationary Emission Control Catalyst Revenue and Market Share by Type (2011-2016)  5.3 Global Stationary Emission Control Catalyst Price by Type (2011-2016)  5.4 Global Stationary Emission Control Catalyst Production Growth by Type (2011-2016) 6 Global Stationary Emission Control Catalyst Market Analysis by Application  6.1 Global Stationary Emission Control Catalyst Consumption and Market Share by Application (2011-2016)  6.2 Global Stationary Emission Control Catalyst Consumption Growth Rate by Application (2011-2016)  6.3 Market Drivers and Opportunities  6.3.1 Potential Applications  6.3.2 Emerging Markets/Countries 7 Global Stationary Emission Control Catalyst Manufacturers Profiles/Analysis  7.1 Hitachi Zosen Corporation  7.1.1 Company Basic Information, Manufacturing Base and Its Competitors  7.1.2 Stationary Emission Control Catalyst Product Type, Application and Specification  7.1.2.1 Type I  7.1.2.2 Type II  7.1.3 Hitachi Zosen Corporation Stationary Emission Control Catalyst Capacity, Production, Revenue, Price and Gross Margin (2015 and 2016)  7.1.4 Main Business/Business Overview  7.2 Basf  7.2.1 Company Basic Information, Manufacturing Base and Its Competitors  7.2.2 Stationary Emission Control Catalyst Product Type, Application and Specification  7.2.2.1 Type I  7.2.2.2 Type II  7.2.3 Basf Stationary Emission Control Catalyst Capacity, Production, Revenue, Price and Gross Margin (2015 and 2016)  7.2.4 Main Business/Business Overview  7.3 Cdti Corp  7.3.1 Company Basic Information, Manufacturing Base and Its Competitors  7.3.2 Stationary Emission Control Catalyst Product Type, Application and Specification  7.3.2.1 Type I  7.3.2.2 Type II  7.3.3 Cdti Corp Stationary Emission Control Catalyst Capacity, Production, Revenue, Price and Gross Margin (2015 and 2016)  7.3.4 Main Business/Business Overview  7.4 Haldor Topsoe  7.4.1 Company Basic Information, Manufacturing Base and Its Competitors  7.4.2 Stationary Emission Control Catalyst Product Type, Application and Specification  7.4.2.1 Type I  7.4.2.2 Type II  7.4.3 Haldor Topsoe Stationary Emission Control Catalyst Capacity, Production, Revenue, Price and Gross Margin (2015 and 2016)  7.4.4 Main Business/Business Overview  7.5 Nikki Universal Co., Ltd.  7.5.1 Company Basic Information, Manufacturing Base and Its Competitors  7.5.2 Stationary Emission Control Catalyst Product Type, Application and Specification  7.5.2.1 Type I  7.5.2.2 Type II  7.5.3 Nikki Universal Co., Ltd. Stationary Emission Control Catalyst Capacity, Production, Revenue, Price and Gross Margin (2015 and 2016)  7.5.4 Main Business/Business Overview  7.6 Jgc C&C  7.6.1 Company Basic Information, Manufacturing Base and Its Competitors  7.6.2 Stationary Emission Control Catalyst Product Type, Application and Specification  7.6.2.1 Type I  7.6.2.2 Type II  7.6.3 Jgc C&C Stationary Emission Control Catalyst Capacity, Production, Revenue, Price and Gross Margin (2015 and 2016)  7.6.4 Main Business/Business Overview  7.7 Cormetech Inc.  7.7.1 Company Basic Information, Manufacturing Base and Its Competitors  7.7.2 Stationary Emission Control Catalyst Product Type, Application and Specification  7.7.2.1 Type I  7.7.2.2 Type II  7.7.3 Cormetech Inc. Stationary Emission Control Catalyst Capacity, Production, Revenue, Price and Gross Margin (2015 and 2016)  7.7.4 Main Business/Business Overview  7.8 Dcl International, Inc.  7.8.1 Company Basic Information, Manufacturing Base and Its Competitors  7.8.2 Stationary Emission Control Catalyst Product Type, Application and Specification  7.8.2.1 Type I  7.8.2.2 Type II  7.8.3 Dcl International, Inc. Stationary Emission Control Catalyst Capacity, Production, Revenue, Price and Gross Margin (2015 and 2016)  7.8.4 Main Business/Business Overview  7.9 Porzellanfabrik Frauenthal Gmbh  7.9.1 Company Basic Information, Manufacturing Base and Its Competitors  7.9.2 Stationary Emission Control Catalyst Product Type, Application and Specification  7.9.2.1 Type I  7.9.2.2 Type II  7.9.3 Porzellanfabrik Frauenthal Gmbh Stationary Emission Control Catalyst Capacity, Production, Revenue, Price and Gross Margin (2015 and 2016)  7.9.4 Main Business/Business Overview  7.10 Honeywell Uop  7.10.1 Company Basic Information, Manufacturing Base and Its Competitors  7.10.2 Stationary Emission Control Catalyst Product Type, Application and Specification  7.10.2.1 Type I  7.10.2.2 Type II  7.10.3 Honeywell Uop Stationary Emission Control Catalyst Capacity, Production, Revenue, Price and Gross Margin (2015 and 2016)  7.10.4 Main Business/Business Overview  7.11 Johnson Matthey Plc  7.12 Corning Inc. 8 Stationary Emission Control Catalyst Manufacturing Cost Analysis  8.1 Stationary Emission Control Catalyst Key Raw Materials Analysis  8.1.1 Key Raw Materials  8.1.2 Price Trend of Key Raw Materials  8.1.3 Key Suppliers of Raw Materials  8.1.4 Market Concentration Rate of Raw Materials  8.2 Proportion of Manufacturing Cost Structure  8.2.1 Raw Materials  8.2.2 Labor Cost  8.2.3 Manufacturing Expenses  8.3 Manufacturing Process Analysis of Stationary Emission Control Catalyst 9 Industrial Chain, Sourcing Strategy and Downstream Buyers  9.1 Stationary Emission Control Catalyst Industrial Chain Analysis  9.2 Upstream Raw Materials Sourcing  9.3 Raw Materials Sources of Stationary Emission Control Catalyst Major Manufacturers in 2015  9.4 Downstream Buyers 12 Global Stationary Emission Control Catalyst Market Forecast (2016-2021)  12.1 Global Stationary Emission Control Catalyst Capacity, Production, Revenue Forecast (2016-2021)  12.2 Global Stationary Emission Control Catalyst Production, Consumption Forecast by Regions (2016-2021)  12.3 Global Stationary Emission Control Catalyst Production Forecast by Type (2016-2021)  12.4 Global Stationary Emission Control Catalyst Consumption Forecast by Application (2016-2021)  12.5 Stationary Emission Control Catalyst Price Forecast (2016-2021)


Tada S.,University of Tokyo | Tada S.,Japan Society for the Promotion of Science | Kikuchi R.,University of Tokyo | Wada K.,Toshiba Corporation | And 4 more authors.
Journal of Power Sources | Year: 2014

Selective CO methanation was carried out over 10 wt%Ni/TiO2 and 0.5 wt%Ru-10 wt%Ni/TiO2, and the durability was examined. During the long-term test, both catalysts abated CO concentration from 0.25% (dry base) to less than 0.05% above ca. 175 °C with CO2 methanation suppressed. Ru-Ni/TiO2 exhibited the high activity of CO methanation compared to Ni/TiO2 during the test. Furthermore, for more than 5500 h, Ru-Ni/TiO2 maintained a wide temperature window for selective CO methanation (>50 °C), where CO and CH4 concentrations were <0.05% and <1%, respectively, at a high gas hourly space velocity of 10,000 h-1. Over Ni/TiO2 and Ru-Ni/TiO2, CO2 methanation activity was initially enhanced, and then stabilized. The initial promotion of CO2 methanation activity is possibly due to the reduction of NiO which remained unreduced after the prereduction by H 2 at 450 °C. © 2014 Elsevier B.V. All rights reserved.


Tada S.,University of Tokyo | Tada S.,Japan Society for the Promotion of Science | Minori D.,University of Tokyo | Otsuka F.,University of Tokyo | And 4 more authors.
Fuel | Year: 2014

The removal of CO from hydrogen-rich gas produced by steam reforming of hydrocarbons by selective CO methanation was investigated over xwt%Ru-ywt%Ni/TiO2 (x = 0, 0.2, 0.3, 0.4, y = 0, 5, 9). The bimetallic catalyst Ru-Ni/TiO2 exhibited higher activity of CO methanation at low temperatures and lower activity of CO2 methanation at high temperatures than Ru/TiO2. Especially, 0.2 wt%Ru-9 wt%Ni/TiO2 was the most suitable catalyst for selective CO methanation. As for the prepared Ru-Ni/TiO2 catalysts, the reverse water gas shift (RWGS) reaction was accelerated with an increase in the Ru loadings. Consequently the 0.2 wt%Ru-9 wt%Ni/TiO2 produced little CO due to the low activity of RWGS reaction, resulting in rapid abatement of CO at low temperatures and low production of CH4 at high temperatures compared to 0.3 wt%Ru-9 wt%Ni/TiO2 and 0.4 wt%Ru-9 wt%Ni/TiO 2. © 2014 Elsevier Ltd. All rights reserved.


Patent
Nikki Universal Co | Date: 2014-12-25

An ammonia decomposition catalyst to be used for an ammonia exhaust gas having a high moisture content; and a method for purifying the ammonia exhaust gas. An ammonia decomposition catalyst for treating an ammonia exhaust gas containing moisture, the catalyst comprising: a lower layer having a noble metal, an inorganic oxide, phosphorus, and a first proton type zeolite or a first ion exchange type zeolite ion-exchanged with Cu, Co or Fe ions; and an upper layer provided on the lower layer and having a second proton type zeolite or a second ion exchange type zeolite ion-exchanged with Cu, Co or Fe ions.


Patent
Nikki Universal Co | Date: 2016-11-02

An ammonia decomposition catalyst to be used for an ammonia exhaust gas having a high moisture content; and a method for purifying the ammonia exhaust gas. An ammonia decomposition catalyst for treating an ammonia exhaust gas containing moisture, the catalyst comprising: a lower layer having a noble metal, an inorganic oxide, phosphorus, and a first proton type zeolite or a first ion exchange type zeolite ion-exchanged with Cu, Co or Fe ions; and an upper layer provided on the lower layer and having a second proton type zeolite or a second ion exchange type zeolite ion-exchanged with Cu, Co or Fe ions.


A catalyst composition of excellent silicon-resistant performance, and a catalyst containing the catalyst composition are provided. The catalyst composition is one for purifying an exhaust gas containing an organic compound, the catalyst composition comprising at least one inorganic oxide (component 1) selected from the group consisting of alumina, zirconia, titania, silica, ceria, and ceria-zirconia, each having a noble metal supported thereon; zeolite (component 2) having supported thereon at least one metal selected from the group consisting of Fe, Cu, Co and Ni; and a PtFe composite oxide (component 3).


Patent
Nikki Universal Co and Hitachi - GE Nuclear Energy | Date: 2011-04-27

A recombination apparatus is provided to an off-gas system of a boiling water nuclear plant. An off-gas system pipe connected to a condenser is connected to the recombination apparatus. A catalyst layer filled with a catalyst for recombining hydrogen and oxygen is disposed in the recombination apparatus. The recombination catalyst has a percentage of the number of Pt particles whose diameters are in a range from more than 1 nm to not more than 3 nm to the numbers of Pt particles whose diameters are in a range from more than 0 nm to not more than 20 nm, falling within a range from 20 to 100%. The condenser discharges gas containing an organosilicon compound (ex. D5), hydrogen, and oxygen, which is introduced to the recombination apparatus. Use of the above recombination catalyst can improve the performance of recombining hydrogen and oxygen more than conventional catalysts and the initial performance of the catalyst can be maintained for a longer period of time.

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