Low Pressure Adsorbent for Recovery & Storage Vented Hydrogen, Phase I

Metadata Updated: November 12, 2020

A high performance fullerene-based adsorbent is proposed for recovery and storage hydrogen and separating helium via pressure-swing-adsorption (PSA) process. Research work performed at MER showed that the proposed adsorbent has an exceptionally high hydrogen adsorption capacity at low pressure and excellent separation factor relative to helium. During the Phase I program, the feasibility of using fullerene-based adsorbents for low-pressure recovery and storage will be determined. The H2/He separation factor, the purity of He, and the economics of the system will also be determined. The performance and cost of conceptual system, producing about 1000 to 100,000 gallon per day, will be estimated and compared to alternative system to demonstrate feasibility.

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Public: This dataset is intended for public access and use. License: No license information was provided. If this work was prepared by an officer or employee of the United States government as part of that person's official duties it is considered a U.S. Government Work.

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Dates

Metadata Created Date November 12, 2020
Metadata Updated Date November 12, 2020

Metadata Source

Harvested from NASA Data.json

Additional Metadata

Resource Type Dataset
Metadata Created Date November 12, 2020
Metadata Updated Date November 12, 2020
Publisher Space Technology Mission Directorate
Unique Identifier Unknown
Maintainer
Identifier TECHPORT_7132
Data First Published 2002-05-01
Data Last Modified 2020-01-29
Public Access Level public
Bureau Code 026:00
Metadata Context https://project-open-data.cio.gov/v1.1/schema/catalog.jsonld
Metadata Catalog ID https://data.nasa.gov/data.json
Schema Version https://project-open-data.cio.gov/v1.1/schema
Catalog Describedby https://project-open-data.cio.gov/v1.1/schema/catalog.json
Homepage URL https://techport.nasa.gov/view/7132
Program Code 026:027
Source Datajson Identifier True
Source Hash f58c59f458717eff239186bee90f43140f2ad0a0
Source Schema Version 1.1

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