Sentence examples for hydrogen facilities from inspiring English sources

The development of a set of safety codes and standards for hydrogen facilities is necessary to ensure they are designed and operated safely.

The environment and energy minister, Simon Corbell, recently announced that the two companies – Spain's Union Fenosa and France's Neoen – that won bids to provide electricity to build large wind farms to supply the ACT will invest $180m to develop hydrogen facilities.

In spite of its wide flammability and sensitivity to ignition and detonation initiation, it is felt that hydrogen can be produced, stored and handled safely with the appropriate considerations in the design of the hydrogen facilities.

The objectives of the optimization problem are: (i) the maximization of the net present value (NPV) and (ii) the minimization of the greenhouse gas (GHG) emissions, while determining: (i) the locations of the hydrogen facilities, (ii) the production technology, (iii) the size of each facility (iv) transportation unit and (v) the distribution route.

To help ensure that a hydrogen facility meets an acceptable level of risk, code and standard development organizations (SDOs) are utilizing risk-informed concepts in developing hydrogen codes and standards.

The result shows that distributed production, and mass storage and transportation via liquefied hydrogen facility are relatively safer than centralized production, and compressed-gaseous hydrogen storage and transportation, respectively.

To ensure that a hydrogen facility is indeed safe, the code and standard requirements should be identified using a risk-informed process that utilizes an acceptable level of risk.

Subsequently, a com 1 putational fluid dynamic (CFD) model of the reformer developed in Tran et al. (2017b) is used to represent the on-line unit at the SMR-based hydrogen facility and is used to characterize the previously unstudied dynamic behavior of the reformer, based on which we develop an optimal strategy to implement the optimized total fuel flow rate to maximize the reformer throughput.

This paper focuses on the development of a real-time furnace-balancing scheme for a reformer at a centralized hydrogen facility using steam methane reforming (SMR) technology so that the reformer fuel input can be optimized in real-time to increase the plant throughput and to reject operational disturbances associated with flow control valves.

As part of the strategies to reduce greenhouse gas emissions, new designs need to be developed to integrate hydrogen production facilities that are based on natural gas reforming with carbon capture facilities.

At this time, hydrogen-based power plants and large hydrogen production facilities are capital intensive and unable to compete financially against hydrocarbon-based energy production facilities.