1,721,120 research outputs found

    Devolatilizzazione e combustione di singole particelle di una lignite italiana

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    The devolatilization and combustion of single particles of an Italian lignite has been observed for different particles diameters and air flow temperatures: a low volatile content bituminous Polish coal has been studied for comparison

    Plasma B-endorphin resistance to dexamethasone suppression in obese patients

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    Patients with simple exogenous obesity are characterized by increased B-endorphin (B-EP) plasma levels, despite normal ACTH and B-Lipotropin (B-LPH). To evaluate the origin of such an hyperendorphinemia, 42 obese patients were submitted to a short overnight dexamethasone suppression test (DST: 1 mg at 23:00 h). Blood samples were taken in basal conditions and 9, and 17 h after DST. The same procedure was applied in 12 healthy, normal weight volunteers. In further five patients, 0.5 mg per 4/die were given. B-EP was measured by radioimmunoassay (RIA) after silicic acid extraction and Sephadex G-75 column chromatography. ACTH and Cortisol were measured by direct IRMA and RIA, respectively. Basal B-EP levels of patients (24.2 +/- 16.5, fmol/ml, M +/- SD) were double than in normal weight controls (10.8 +/- 4.6), while ACTH and cortisol fell in the normal range. ACTH and cortisol were significantly reduced by DST in both patients and controls, while B-EP in patients did not. Cortisol, however, was not suppressed in 7 patients (16%). At 08:00, the suppression of B-EP in controls was 49.0 +/- 18.4%, while in obese patients it was only 21.2 +/- 38.8% (p less than 0.01). However, patients with weight excess below 50% normally suppressed B-EP (41.6 +/- 15.3%), while those with weight excess over 75% did not (11.3 +/- 47.5%). The doubling of dexamethasone intake does not lead to a suppression of plasma B-EP in these last patients. These data indicate the existence of neuroendocrine abnormalities in the hypothalamus-pituitary-adrenal axis of obese patients and suggest that their hyperendorphinemia originates outside the anterior pituitary

    Going Beyond Counting First Authors in Author Co-citation Analysis

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    The present study examines one of the fundamental aspects of author co-citation analysis (ACA) - the way co-citation counts are defined. Co-citation counting provides the data on which all subsequent statistical analyses and mappings are based, and we compare ACA results based on two different types of co-citation counting - the traditional type that only counts the first one among a cited work's authors on the one hand and a non-traditional type that takes into account the first 5 authors of a cited work on the other hand. Results indicate that the picture produced through this non-traditional author co-citation counting contains more coherent author groups and is therefore considerably clearer. However, this picture represents fewer specialties in the research field being studied than that produced through the traditional first-author co-citation counting when the same number of top-ranked authors is selected and analyzed. Reasons for these effects are discussed

    Optimal design of direct expansion systems for electricity production by LNG cold energy recovery

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    The aim of this paper is the investigation of cold energy recovery of liquefied natural gas (LNG) in regasification terminals achievable through direct expansion techniques. After an overview of the state of the art related to the LNG system and the technologies proposed for power recovery, multi-pressure direct expansion solutions with internal heat recovery (multi-pressure DE) are analysed. The purpose is to identify the highest level of recoverable energy and the optimal design parameters, considering technological constraints such as pressure and minimum end-expansion temperature. The multi-pressure DE solutions prove to be innovative power recovery methods because, with a relatively low use of seawater, it is possible to save regasified LNG and generate electrical power, valorising the energy invested in liquefaction. An estimate of recoverable power in operating terminals is carried out. Configurations with cryogenic or non-cryogenic turboexpanders are discussed. Using the proposed solution with non-cryogenic turboexpander and distribution pressure of 3.5 MPa, 56 kJ for each kg of LNG can be produced, which can become more than 150 kJ/kg with cryogenic turboexpanders. For long-distance distribution, cryogenic multi-pressure DE cycles can recover around 100-120 kJ per kg of LNG. The presented techniques can allow recovery of up to and over 30% of the maximum specific work available in LNG regasification

    Routes for Hydrogen Introduction in the Industrial Hard-to-Abate Sectors for Promoting Energy Transition

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    This paper offers a set of comprehensive guidelines aimed at facilitating the widespread adoption of hydrogen in the industrial hard-to-abate sectors. The authors begin by conducting a detailed analysis of these sectors, providing an overview of their unique characteristics and challenges. This paper delves into specific elements related to hydrogen technologies, shedding light on their potential applications, and discussing feasible implementation strategies. By exploring the strengths and limitations of each technology, this paper offers valuable insights into its suitability for specific applications. Finally, through a specific analysis focused on the steel sector, the authors provide in-depth information on the potential benefits and challenges associated with hydrogen adoption in this context. By emphasizing the steel sector as a focal point, the authors contribute to a more nuanced understanding of hydrogen's role in decarbonizing industrial processes and inspire further exploration of its applications in other challenging sectors

    Hydrogen Gas Compression for Efficient Storage: Balancing Energy and Increasing Density

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    This article analyzes the processes of compressing hydrogen in the gaseous state, an aspect considered important due to its contribution to the greater diffusion of hydrogen in both the civil and industrial sectors. This article begins by providing a concise overview and comparison of diverse hydrogen-storage methodologies, laying the groundwork with an in-depth analysis of hydrogen’s thermophysical properties. It scrutinizes plausible configurations for hydrogen compression, aiming to strike a delicate balance between energy consumption, derived from the fuel itself, and the requisite number of compression stages. Notably, to render hydrogen storage competitive in terms of volume, pressures of at least 350 bar are deemed essential, albeit at an energy cost amounting to approximately 10% of the fuel’s calorific value. Multi-stage compression emerges as a crucial strategy, not solely for energy efficiency, but also to curtail temperature rises, with an upper limit set at 200 °C. This nuanced approach is underlined by the exploration of compression levels commonly cited in the literature, particularly 350 bar and 700 bar. The study advocates for a three-stage compression system as a pragmatic compromise, capable of achieving high-pressure solutions while keeping compression work below 10 MJ/kg, a threshold indicative of sustainable energy utilization
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