Hydrogen Via Water Electrolysis Cost Analysis Hydrogen E31a PDF Download

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Hydrogen via Water Electrolysis - Cost Analysis - Hydrogen E31A

Hydrogen via Water Electrolysis - Cost Analysis - Hydrogen E31A
Author: Intratec
Publisher: Intratec
Total Pages: 102
Release: 2019-09-17
Genre: Business & Economics
ISBN:

Download Hydrogen via Water Electrolysis - Cost Analysis - Hydrogen E31A Book in PDF, ePub and Kindle

This report presents a cost analysis of Hydrogen production from water. The process examined is a typical electrolysis process. In this process, electricity is used to split water into Hydrogen and oxygen. This report was developed based essentially on the following reference(s): "Hydrogen", Kirk-Othmer Encyclopedia of Chemical Technology, 5th edition Keywords: Electrolytic H2, Electrolyzer, Fuel Cell


Isopropyl Alcohol Production from Acetone - Cost Analysis - Isopropanol E31A

Isopropyl Alcohol Production from Acetone - Cost Analysis - Isopropanol E31A
Author: Intratec
Publisher: Intratec Solutions
Total Pages: 104
Release: 2019-09-17
Genre: Business & Economics
ISBN:

Download Isopropyl Alcohol Production from Acetone - Cost Analysis - Isopropanol E31A Book in PDF, ePub and Kindle

This report presents a cost analysis of Isopropanol production from acetone. The process examined is a typical acetone hydrogenation process. In this process, acetone hydrogenation is carreid out in liquid phase, in a fixed bed reactor, catalyzed by a Raney nickel catalyst. This report was developed based essentially on the following reference(s): (1) US Patent 8283504, issued to Mitsui Chemicals in 2012 (2) US Patent 20150083578, issued to LG Chem, LTD in 2015 (3) US Patent 6930213, issued to INEOS Phenol GMBH (former Phenolchemie GmbH & Co. KG) in 2006 Keywords: Isopropanol, isopropyl alcohol, IPA, acetone hydrogenation, lummus, polimeri europa, versalis


Hydrogen Production from Water

Hydrogen Production from Water
Author:
Publisher:
Total Pages:
Release: 2021
Genre: Hydrogen
ISBN:

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This report presents the economics of Hydrogen production via water electrolysis. The process examined is an alkaline electrolysis process.The primary objective of this study is to explain the cost structure of the aforementioned process,encompassing capital investment and operating cost figures.


Butanediol Production from Acetylene - Cost Analysis - Butanediol E31A

Butanediol Production from Acetylene - Cost Analysis - Butanediol E31A
Author: Intratec
Publisher: Intratec
Total Pages: 102
Release: 2019-09-17
Genre: Business & Economics
ISBN:

Download Butanediol Production from Acetylene - Cost Analysis - Butanediol E31A Book in PDF, ePub and Kindle

This report presents a cost analysis of 1,4-Butanediol (BDO) production from acetylene and formaldehyde. The process examined is a typical acetylene-based Reppe process. Acetylene and an aqueous solution of formaldehyde (37 wt%) react to produce 1,4-butynediol. The butynediol is then hydrogenated to produce BDO. This report was developed based essentially on the following reference(s): (1) "Butanediols, Butenediol, and Butynediol", Ullmann's Encyclopedia of Industrial Chemistry, 7th edition (2) US Patent 7759531, issued to BASF in 2010 Keywords: BDO, Ethyne, Fixed-Bed Reactor, Catalytic Reactor


Benzene Production from Toluene - Cost Analysis - Benzene E31A

Benzene Production from Toluene - Cost Analysis - Benzene E31A
Author: Intratec
Publisher: Intratec
Total Pages: 102
Release: 2019-09-17
Genre: Business & Economics
ISBN:

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This report presents a cost analysis of Benzene production from toluene. The process examined is a typical selective toluene disproportionation process (STDP). In the STDP, toluene is converted into benzene and xylenes (mainly, p-xylene). Benzene is recovered from the reactor output via distillation and p-Xylene is separated as a by-product using a crystallization unit. This report was developed based essentially on the following reference(s): (1) US Patent 7230152, issued to UOP in 2007 (2) US Patent 4097543, issued to ExxonMobil in 1978 Keywords: Aromatics, BTX, ExxonMobil PxMax, UOP Px Plus, GTC GT-STDP


Propylene Oxide from Propylene and Ethylbenzene - Cost Analysis - Propylene Oxide E31A

Propylene Oxide from Propylene and Ethylbenzene - Cost Analysis - Propylene Oxide E31A
Author: Intratec
Publisher: Intratec
Total Pages: 103
Release: 2019-09-17
Genre: Business & Economics
ISBN:

Download Propylene Oxide from Propylene and Ethylbenzene - Cost Analysis - Propylene Oxide E31A Book in PDF, ePub and Kindle

This report presents a cost analysis of Propylene Oxide (PO) production from chemical grade (CG) propylene and ethylbenzene. The process examined is similar to LyondellBasell process. In this process, ethylbenzene is oxidized to produce ethylbenzene hydroperoxide, which reacts with propylene to produce Propylene Oxide. Styrene is generated as by-product in the process. This report was developed based essentially on the following reference(s): "Propylene Oxide", Ullmann's Encyclopedia of Industrial Chemistry, 7th edition Keywords: Propene, Ethylbenzol, Oxidation, Epoxidation, EBHP, Phenylethene, POSM


Manufacturing Cost Analysis for Proton Exchange Membrane Water Electrolyzers

Manufacturing Cost Analysis for Proton Exchange Membrane Water Electrolyzers
Author:
Publisher:
Total Pages: 0
Release: 2019
Genre:
ISBN:

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Hydrogen is produced by several means including water electrolysis where water molecules are split into hydrogen and oxygen. While there are several commercial electrolysis systems, proton exchange membrane (PEM) technology has emerged as a technology of choice in the last decade or so because of the versatile properties it possesses. High current and power densities and high efficiency values are among the advantages of the PEM electrolyzer over other commercial or near-commercial electrolysis systems such as alkaline or solid oxide. This study attempts to study the impact of manufacturing economies of scale on the cost of the PEM electrolyzer and how this can be linked to reducing the cost of hydrogen production. We found that adoption of the high throughput, automated manufacturing processes that have high process yields such as roll-to-roll manufacturing of catalyst coated membrane and advanced coating processes for metal plates, could push the cost for the PEM electrolyzer stack to the $323/kW level for an overall production volume of 10MW (e.g. 1 MW systems x 10 units/year). The stack cost can be pushed as low as $165/kW at 10,000 systems/year. We do not expect to see same rate of the cost reduction in the balance of plant because most parts are outsourced from part suppliers who offer limited discounts on their products. System cost including stack and balance of plant, could also be pushed down with economies of scale. The uninstalled system cost can be reduced from $515/kW at 10 units/year to $230/kW at 10,000 units/year.


Epichlorohydrin Production from Glycerol - Cost Analysis - ECH E31A

Epichlorohydrin Production from Glycerol - Cost Analysis - ECH E31A
Author: Intratec
Publisher: Intratec
Total Pages: 102
Release: 2019-09-17
Genre: Business & Economics
ISBN:

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This report presents a cost analysis of Epichlorohydrin production from crude glycerol. The process under analysis involves two main steps: hydrochlorination of glycerol to dichlorohydrins (DCH); and alkaline dehydrochlorination of DCH to Epichlorohydrin. This report was developed based essentially on the following reference(s): EP Patent 2219779, issued to Conser in 2012 Keywords: hydrochlorination, dichlorohydrins, DCH, dichloropropanol, DCP, alkaline dehydrochlorination, CONSER, Dow, Solvay, KVT


Hydrogen via Natural Gas Steam Reforming - Cost Analysis - Hydrogen E11A

Hydrogen via Natural Gas Steam Reforming - Cost Analysis - Hydrogen E11A
Author: Intratec
Publisher: Intratec
Total Pages: 102
Release: 2019-09-17
Genre: Business & Economics
ISBN:

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This report presents a cost analysis of Hydrogen production from natural gas. The process examined is a typical steam reforming process. This process comprises the following main steps: natural gas steam reforming for syngas production; shift conversion, i.e., reaction of carbon monoxide with steam, producing carbon dioxide and additional Hydrogen; Hydrogen purification by means of a pressure swing adsorption (PSA) system. This report was developed based essentially on the following reference(s): (1) "Hydrogen, 2. Production", Ullmann's Encyclopedia of Industrial Chemistry, 2011 (2) "Hydrogen", Kirk-Othmer Encyclopedia of Chemical Technology, 5th edition Keywords: H2, NG, Water-gas Shifting, Reformer, Steam Methane Reforming, SMR


Wind-To-Hydrogen Project

Wind-To-Hydrogen Project
Author:
Publisher:
Total Pages: 0
Release: 2008
Genre:
ISBN:

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This study is being performed as part of the U.S. Department of Energy and Xcel Energy's Wind-to-Hydrogen Project (Wind2H2) at the National Renewable Energy Laboratory. The general aim of the project is to identify areas for improving the production of hydrogen from renewable energy sources. These areas include both technical development and cost analysis of systems that convert renewable energy to hydrogen via water electrolysis. Increased efficiency and reduced cost will bring about greater market penetration for hydrogen production and application. There are different issues for isolated versus grid-connected systems, however, and these issues must be considered. The manner in which hydrogen production is integrated in the larger energy system will determine its cost feasibility and energy efficiency.