STEAG Energy Services GmbH

Essen, Germany

STEAG Energy Services GmbH

Essen, Germany

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The report covers forecast and analysis for the catalyst regeneration market on a global and regional level. The study provides historic data of 2014 along with a forecast from 2015 to 2020 based on both volumes (kilo tons) and revenue (USD million). The study includes drivers and restraints for the catalyst regeneration market along with the impact they have on the demand over the forecast period. Additionally, the report includes the study of opportunities available in the catalyst regeneration market on a global level. In order to give the users of this report a comprehensive view on the catalyst regeneration market, we have included a detailed value chain analysis. To understand the competitive landscape in the market, an analysis of porter’s five forces model for the catalyst regeneration market has also been included. The study encompasses a market attractiveness analysis, wherein technology segments are benchmarked based on their market size, growth rate and general attractiveness. Request Sample Report: bit.ly/2fWh7Tt The study provides a decisive view on the catalyst regeneration market by segmenting the market based on technology and applications. All the technology and application segments have been analyzed based on present and future trends and the market is estimated from 2014 to 2020. Key technology markets covered under this study include off-site regeneration and on-site regeneration. Petroleum refining, chemical synthesis, polymer and environmental are key application markets for catalyst regeneration. The regional segmentation includes the current and forecast demand for North America, Europe, Asia Pacific, Latin America, and Middle East and Africa with its further, Bifurcation into major countries including U.S., Germany, France, UK, China, Japan, India and Brazil. This segmentation includes demand for catalyst regeneration based on individual technology and applications in all the regions and countries. The report covers detailed competitive outlook including the market share and company profiles of the key participants operating in the global market include Haldor Topsoe, Eurecat U.S. Inc., TriCAT GmbH Catalyst Services, Johnson Matthey PLC, STEAG Energy Services, LLC, Albemarle Corporation, CoaLogix, Inc., Axens S.A., BASF SE, Porocel Adsorbents and Bayer Technology Services GmbH. The detailed description of players includes parameters such as company overview, financial overview, business strategies and SWOT analysis and recent developments of the company. A to Z Research: All Global Energy related reports along with a forecast from 2016 to 2021 based on revenue (USD Billion) bit.ly/2eWbdwQ  This report segments the global catalyst regeneration market as follows: Global Catalyst Regeneration Market: Technology Segment Analysis On-site Off-site Global Catalyst Regeneration Market: Application Segment Analysis Petroleum Refining Chemical Synthesis Polymer Environmental Global Catalyst Regeneration Market: Regional Segment Analysis Browse detail report at: atozresearch.com/global-catalyst-regeneration-market-rese... North America US Europe Germany France UK Asia Pacific China Japan India Latin America Brazil Middle East and Africa AboutA to Z Research A to ZResearchis a single destination for all the industry, company and country reports. We feature large repository of latest industry reports, leading and niche company profiles, and market statistics released by reputed private publishers and public organizations.A to Z Researchis the comprehensive collection of market intelligence products and services available on air. We have market research reports from number of leading publishers and update our collection daily to provide our clients with the instant online access to our database. With access to this database, our clients will be able to benefit from expert insights on global industries, products, and market trends. Contact US 3422 SW 15 Street,Suit #8138, Deerfield Beach,Florida 33442, USA Tel: +1-386-310-3803GMT  Tel: +49-322 210 92714 USA/Canada Toll Free No.1-855-465-465 Email: [email protected] Website: atozresearch.com/


Catalyst Regeneration (On-site and Off-site) Market for Petroleum Refining, Chemical Synthesis, Polymer and Environmental Applications: Global Industry Perspective, Comprehensive Analysis and Forecast, 2014 – 2020 The report covers forecast and analysis for the catalyst regeneration market on a global and regional level. The study provides historic data of 2014 along with a forecast from 2015 to 2020 based on both volumes (kilo tons) and revenue (USD million). The study includes drivers and restraints for the catalyst regeneration market along with the impact they have on the demand over the forecast period. Additionally, the report includes the study of opportunities available in the catalyst regeneration market on a global level. In order to give the users of this report a comprehensive view on the catalyst regeneration market, we have included a detailed value chain analysis. To understand the competitive landscape in the market, an analysis of porter’s five forces model for the catalyst regeneration market has also been included. The study encompasses a market attractiveness analysis, wherein technology segments are benchmarked based on their market size, growth rate and general attractiveness. The study provides a decisive view on the catalyst regeneration market by segmenting the market based on technology and applications. All the technology and application segments have been analyzed based on present and future trends and the market is estimated from 2014 to 2020. Key technology markets covered under this study include off-site regeneration and on-site regeneration. Petroleum refining, chemical synthesis, polymer and environmental are key application markets for catalyst regeneration. The regional segmentation includes the current and forecast demand for North America, Europe, Asia Pacific, Latin America, and Middle East and Africa with its further, Bifurcation into major countries including U.S., Germany, France, UK, China, Japan, India and Brazil. This segmentation includes demand for catalyst regeneration based on individual technology and applications in all the regions and countries. The report covers detailed competitive outlook including the market share and company profiles of the key participants operating in the global market include Haldor Topsoe, Eurecat U.S. Inc., TriCAT GmbH Catalyst Services, Johnson Matthey PLC, STEAG Energy Services, LLC, Albemarle Corporation, CoaLogix, Inc., Axens S.A., BASF SE, Porocel Adsorbents and Bayer Technology Services GmbH. The detailed description of players includes parameters such as company overview, financial overview, business strategies and SWOT analysis and recent developments of the company. This report segments the global catalyst regeneration market as follows:


Simon F.-G.,BAM Federal Institute of Materials Research and Testing | Keldenich K.,STEAG Energy Services GmbH
Chemie-Ingenieur-Technik | Year: 2012

Waste management in Germany covers an amount of 359 million tons. The largest fraction is construction and demolition waste (C&D waste) with some 54 %. The treatment processes for C&D waste differ from those for municipal solid waste. According to the European Directive on Waste a waste hierarchy shall apply where recycling has a higher priority than energy recovery. A thermal treatment is regarded as recovery operation only if the energy efficiency is above a certain limit. Under the terms of the directive a simplified calculation of the energy efficiency is perfomed using the so-called R1 formula. Published data on heat and power production of several thermal waste treatment plants are compared to the R1 formula and data from literature. Amount and waste management options for different waste fractions and how to evaluate different waste management processes are discussed. © 2012 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim.


Wortmann B.,STEAG Energy Services GmbH | Knorr J.,TU Dresden
Applied Radiation and Isotopes | Year: 2012

Background: In 2001 and 2003, at the University of Pavia, Italy, boron neutron capture therapy (BNCT) has been successfully used in the treatment of hepatic colorectal metastases (Pinelli et al., 2002; Zonta et al., 2006). The treatment procedure (TAOrMINA protocol) is characterised by the auto-transplantation and extracorporeal irradiation of the liver using a thermal neutron beam. Methods: The clinical use of this approach requires well founded data and an optimized irradiation facility. In order to start with this work and to decide upon its feasibility at the research reactor TRIGA Mainz, basic data and requirements have been considered (Wortmann, 2008). Computer calculations using the ATTILA (Transpire Inc. 2006) and MCNP (LANL, 2005) codes have been performed, including data from conventional radiation therapy, from the TAOrMINA approach, resulting in reasonable estimations. Results: Basic data and requirements and optimal parameters have been worked out, especially for use at an optimized TRIGA irradiation facility (Wortmann, 2008). Advantages of the extracorporeal irradiation with auto-transplantation and the potential of an optimized irradiation facility could be identified. Within the requirements, turning the explanted organ over by 180° appears preferable to a whole side source, similar to a permanent rotation of the organ. Conclusions: The design study and the parameter optimization confirm the potential of this approach to treat metastases in explanted organs. The results do not represent actual treatment data but a first estimation. Although all specific values refer to the TRIGA Mainz, they may act as a useful guide for other types of neutron sources. The recommended modifications (Wortmann, 2008) show the suitability of TRIGA reactors as a radiation source for BNCT of extracorporeal irradiated and auto-transplanted organs. © 2012 Elsevier Ltd.


Patent
Steag Energy Services Gmbh | Date: 2013-03-13

Methods of removing iron from a catalytic converter having an accumulation of one or more iron compounds and regenerating a catalytic converter are provided. A catalytic converter having an accumulation of one or more iron compounds embedded or deposited thereon can be treated with a substantially aqueous alkaline solution in which the substantially aqueous alkaline solution includes an antioxidant.


Patent
STEAG Energy Services GmbH | Date: 2010-02-24

A method for operating a hybrid power plant comprising fuel-operated heating and solar energy heating of carrier fluids, wherein a first portion of total power provided by the power plant is based on fuel-operated heating of carrier fluids and a second portion of the total power is based on solar energy heating of carrier fluids, the heat absorbed by a solar energy heated carrier fluid is transferred to a carrier fluid circuit of a fuel-operated part of the power plant. When a sudden increase or reduction of the total power provided by the power plant is required as compared to a basic state, the second portion is first increased or reduced over a short time period in order to provide a positive or negative reserve power. Subsequently, the first portion is slowly increased or reduced and the second portion based on solar energy heating is correspondingly reduced or increased again.


Patent
Steag Energy Services Gmbh | Date: 2013-03-14

Methods of removing or softening calcium material from a substrate (e.g., a catalytic converter) and regenerating a catalytic converter are provided. A substrate (e.g., a catalyst support material) having a calcium containing material (e.g., calcium-containing fly ash) embedded or deposited thereon can be treated with a composition including one or more organosulfur oxoacids or salts thereof.


Patent
Steag Energy Services GmbH | Date: 2014-06-13

The invention is directed to a method for the removal of mercury and selenium from sulfate-containing waste water. The method may include the following steps: a) a mercury- and selenium-contaminated waste water with a known sulfate concentration is provided, b) barium sulfate (BaSO_(4)) is precipitated from the provided waste water by the addition of a predefined amount of Ba^(2+) ions to the waste water, c) BaSO_(4 )(if necessary together with other solids) is separated obtaining a low-solid waste water, d) the low-solid waste water is fed to an ion exchanger for the removal of mercury obtaining a waste water with a reduced mercury content, e) selenium and/or selenium compounds are removed from the waste water with the reduced mercury content and f) a sulfate-containing solution or solid is added to the waste water with a reduced selenium and/or selenium compound content in order to precipitate barium sulfate.


Patent
STEAG Energy Services GmbH | Date: 2012-04-03

A method for treating a catalyst base that comprises a contact area of porous material. A fluid, such as a flue gas stream, can be conducted along the contact area. A catalytically relevant substance is introduced into pores of the catalyst base using a transport fluid and remains on pore wall areas after removal of the transport fluid. The introduction is carried out such that an amount of the catalytically relevant substance relative to the surface remains on the pore wall areas as a function of location within the pore and decreases within the pore after exceeding a specific pore depth. A blocking fluid can first be introduced into pore regions beyond the specific pore depth, thus blocking these regions when transport fluid containing the catalytically relevant substance is introduced.


The method according to the invention provides a method for treating a waste water, where (a) the waste water is provided having specific sulfate, chloride, mercury, and selenium concentrations, (b) the waste water (WW) is fed to a high pressure separator 1 using a high-pressure pump (P1) in which the waste water (WW) is separated into a permeate volume (PV) containing reduced sulfate, chloride, mercury, and selenium concentrations and a concentrate volume (CV), (c) and where the concentrate volume (CV) is separated using a cleaning apparatus 4 that reduces both mercury and selenium in the concentrate volume.

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