cometadata/datacite-titles-descriptions-related-identifiers huggingface dataset:
DOI: 10.17632/fr9t5fkkvz.1
title: Olive oil geography by GC-IMS analysis

description: 53 olive oils from Spain (20), Italy (20) and Greece (13) of extra virgin quality, harvested during the 2014/2015 season, were kindly supplied by Coop Switzerland (Basel, Switzerland). Authenticity was verified by the supplier by chemical and isotope analysis.
Olive oil samples were analysed by headspace GC-IMS. The setup includes an Agilent 6890N gas chromatograph (Agilent Technologies, Palo Alto, USA), coupled with a standalone ion mobility spectrometer (Gesellschaft für Analytische Sensorsysteme mbH, Dortmund, Germany). Measurements were carried out in triplicates.
Binary files (*.mea format G.A.S. Sensorsysteme m.b.H., Dortmund, Germany)
DOI: 10.17632/hbbyzcrzy4.1
title: Why Integer Ratios Trigger the Illusion of Proportionality: Examining the Underlying Mechanism and Its Neurocognitive Basis

description: All raw and processed data were uploaded except for the ERP raw data. All the variable names are translated into English, please contact the author to retrieve detailed descriptions of the data if necessary.
DOI: 10.17632/mnpv3mmftz.1
title: Saitta et al.

description: Data used for the manuscript "Effect of leaf trichomes in different species of Cucurbitaceae on attachment ability of the melon ladybird beetle Chnootriba elaterii". In particular data regarding trichome density, trichome dimensions, normal friction force of the larvae, normal friction force of adults
DOI: 10.17632/982k4xhj5t.1
title: Data of Geochronology and geochemistry of Upper Paleozoic sandstones at Tiekelike, NW China: Implications for the tectonic evolution of the southwestern margin of the Tarim Block

description: Table 1. Sample location of the studied Upper Paleozoic sandstones (QF, KF, and TF) from the Tiekelike Uplift.
Table 2. Sample location of the studied sandstones used for zircon U–Pb geochronology.
Table 3. Major elements (wt%), trace elements (ppm), REE (ppm) and element ratios of the studied Upper Paleozoic sandstones from the Tiekelike Uplift in comparison to the average compositions of international sediments from references. 
Table 4. LA–ICP–MS U–Pb isotopic data for detrital zircons from the studied Upper Paleozoic sandstones from the Tiekelike Uplift.
Table 5. Detailed explanation of zircon U–Pb ages, Th/U ratios, and zircon morphology and texture for every cluster ages of the QF, KF, and TF, respectively.
Table 6. Comparison of elemental ratios of QF, KF, and TF sandstones with similar ratios from felsic rocks, mafic rocks, and upper continental crust.
Table 7. Geochronological data of the granitoids, sedimentary and metamorphic rocks from the Tiekelike Tectonic Belt and the Western Kunlun Orogenic Belt.
DOI: 10.17632/jh9mk3c583.1
title: circSPECC1 western blot

description: Original western blot
DOI: 10.17632/jh9mk3c583.2
title: circSPECC1 western blot

description: Original western blot
DOI: 10.17632/fshtbhffth.1
title: A dataset of sensory perception of chocolates, guacamoles, ice teas and crisps collected with consumers using six temporal methods.

description: This article describes a dataset providing temporal sensory perception data of four dark chocolates, four guacamoles, four crisps and four ice teas collected from 436 consumers divided in six groups. Each group of consumers described the products using a different sensory method among: Temporal Dominance of Sensations (TDS), Temporal Check-All-That-Apply (TCATA), Attack-Evolution-Finish (AEF) dominance, AEF applicability, Free-Comment Attack-Evolution-Finish (FC-AEF) dominance and FC-AEF applicability. Each consumer evaluated all the products: guacamoles and ice tea were evaluated in the lab in one session; chocolates and crisps were evaluated at home in two separate sessions. Within each product category, one sample has been replicated. The consumers started with product descriptions, then they gave a hedonic score, and after having tasted all the products related to a same category, they answered questions about products complexity and difficulty of the task. Consumer information included in the dataset is sex, age and frequency of consumption of each product category. This dataset is unique as it addresses several temporal methods applied on four product categories with different textures and levels of complexity. Thus, it could be very useful for the sensometric community to compare the different methods and their parameters: dominance vs. applicability, periods vs. continuous time, simultaneous vs. retrospective measures, list of terms vs. Free-Comment.
DOI: 10.17632/fshtbhffth.2
title: A dataset of sensory perception of chocolates, guacamoles, ice teas and crisps collected with consumers using six temporal methods.

description: This article describes a dataset providing temporal sensory perception data of four dark chocolates, four guacamoles, four crisps and four ice teas collected from 436 consumers divided in six groups. Each group of consumers described the products using a different sensory method among: Temporal Dominance of Sensations (TDS), Temporal Check-All-That-Apply (TCATA), Attack-Evolution-Finish (AEF) dominance, AEF applicability, Free-Comment Attack-Evolution-Finish (FC-AEF) dominance and FC-AEF applicability. Each consumer evaluated all the products: guacamoles and ice tea were evaluated in the lab in one session; chocolates and crisps were evaluated at home in two separate sessions. Within each product category, one sample has been replicated. The consumers started with product descriptions, then they gave a hedonic score, and after having tasted all the products related to a same category, they answered questions about products complexity and difficulty of the task. Consumer information included in the dataset is sex, age and frequency of consumption of each product category. This dataset is unique as it addresses several temporal methods applied on four product categories with different textures and levels of complexity. Thus, it could be very useful for the sensometric community to compare the different methods and their parameters: dominance vs. applicability, periods vs. continuous time, simultaneous vs. retrospective measures, list of terms vs. Free-Comment.
DOI: 10.17632/mjfv43zgtv.1
title:  All original wav files that were used in the study

description:  All original wav files that were used in the study
DOI: 10.17632/mjfv43zgtv.2
title:  All original wav files that were used in the study

description:  Files description:
1. phrase.rar- Examples for original wav files. All wav files can be found in Prat et al. Scientific data 2017
2.- 326 sentences.txt - The 512-dimensions encodings of the 326 annotated sequences used in the study. Context and individual appear the the beginning of each sequence 
3. encodings.csv - The encodings of all individual syllables (>28,000) used to train the VAE
4. realanno - The context annotations of all individual syllables
DOI: 10.17632/mjfv43zgtv.3
title:  All original wav files that were used in the study

description:  Files description:
1. phrase.rar- Examples for original wav files. All wav files can be found in Prat et al. Scientific data 2017
2.- 326 sentences.txt - The 512-dimensions encodings of the 326 annotated sequences used in the study. Context and individual appear the the beginning of each sequence 
3. encodings.csv - The encodings of all individual syllables (>28,000) used to train the VAE
4. realanno - The context annotations of all individual syllables
DOI: 10.17632/38tn7gkgsh.1
title: Electrical Resistivity Tomography datasets for landslide detection. A case study in Tghat-Fez (Morocco)

description: The application of the Electrical resistivity tomography (ERT) Method, in conjunction with the BERT python-based inversion approach, leads to the development of a dependable methodology for fault and landslide identification.

The 2D ERT data were collected along nine profiles. The dipole-dipole array configuration was used with electrode spacing of 2 m and an overall length of 96 m, reaching a depth of aproximatly 20 m.
DOI: 10.17632/rh8rm79g23.1
title: Print media data

description: Data used for simulation in paper titled - Reducing the Supply Chain Bullwhip effect in print media: A system dynamics-based approach
DOI: 10.17632/3r643by58z.1
title: LINF_330018400

description: guanylate kinase
Leishmania infantum (strain JPCM5)
DOI: 10.17632/gtfbhn8n3m.1
title: LINF_330019300

description: protein of unknown function - conserved
Leishmania infantum (strain JPCM5)
DOI: 10.17632/ynmtfpk545.1
title: LINF_330019100

description: pumilio protein 6 | PUF6
Leishmania infantum (strain JPCM5)
DOI: 10.17632/z4b83y7c6n.1
title: The effect of wall thermal conductivity on the dimensionless Sherwood number in microchannel reactors designed with reforming catalyst segmentation methods

description: The dimensionless Sherwood number data are presented to illustrated the effect of wall thermal conductivity on the mass-transfer operation of microchannel reactors designed with reforming catalyst segmentation methods. The dimensionless Sherwood number is a dimensionless number used in mass-transfer operation. The dimensionless Sherwood number represents the ratio of the convective mass transfer to the rate of diffusive mass transport. The microchannel reactor is configured for simultaneous oxidation and steam reformation of methanol. The reforming process proceeds in one set of the channels through which the endothermic reactants flow, and the exothermic oxidation process proceeds in the second set of the channels. The ratio of the height of the channels to the width of the channels may vary. The channels are 0.7 millimeters in height and in width and 30.0 millimeters in length. The oxidation catalyst consists essentially of oxides of copper, zinc and aluminum. The oxidation catalyst allows for initial start-up and the heat-up of the reactor system. The reforming catalyst consists essentially of copper and oxides of zinc and aluminum. The exothermic and endothermic processes are conducted at a pressure of 0.8 megapascals, with a methanol-air equivalence ratio of 0.8 and a steam-to-methanol molar ratio of 1.17. The inlet temperature of the mixtures is 373 degrees Kelvin. The temperature of the reactor can be regulated by the balance of the flow rates so that the catalyst is not overheated by the exothermic process and thus damaged. The gas velocity is 2.0 meters per second at the reforming channel inlets and 0.6 meters per second at the oxidation channel inlets, thereby assuring sufficient heat in the reactor to carry out endothermic reforming of methanol. The boundary conditions relate macroscopic fluid flow at a catalytically active surface to the rates of surface reactions. In each exothermic oxidation channel, the catalyst layer is reduced by half in amount. The catalyst segments have a uniform distribution of length, and the spacing between catalyst segments is equal to their length. To obtain the solution of the problem, numerical simulations are performed using fluid mechanics. The mass fluxes of gas-phase species at the phase boundaries are balanced by the production rates of gas-phase species by surface reactions. Heat fluxes in the solid phase are balanced by chemical heat release at the surface. The energy released or consumed at each phase boundary is obtained using a summation over all gas-phase species.
Contributor: Junjie Chen, E-mail address: koncjj@gmail.com, ORCID: 0000-0002-5022-6863, Department of Energy and Power Engineering, School of Mechanical and Power Engineering, Henan Polytechnic University, 2000 Century Avenue, Jiaozuo, Henan, 454000, P.R. China
DOI: 10.17632/hnbkj5z7c3.1
title: LINF_330018200

description: protein of unknown function - conserved
Leishmania infantum (strain JPCM5)
DOI: 10.17632/cb8kzcrcr2.1
title: Thermodynamic data at extremely high flow velocities pertaining to catalytically stabilized combustion systems with highly conductive materials

description: The thermodynamic data at extremely high flow velocities are obtained for catalytically stabilized combustion systems with highly conductive materials. The catalyst in the catalytically stabilized combustion system generally operates at a temperature approximating the theoretical adiabatic flame temperature of the fuel-air admixture charged to the combustion zone. The entire catalyst may not be at these temperatures, but preferably a major portion, or essentially all, of the catalyst surface is at such operating temperatures. The temperature of the catalyst zone is controlled by controlling the composition and initial temperature of the fuel-air admixture as well as the uniformity of the mixture. The residence time is governed largely by temperature, pressure and space throughput, and generally is measured in milliseconds. The volume of catalyst is taken as the total superficial volume encompassing the active catalyst and any less active support, including any voids or gas passages through the catalyst. The catalytically stabilized combustion system comprises a concentric annular channel, wherein the concentric annular channel further comprises an inner annular channel and an outer annular channel. The concentrically arranged annular channel is 5.0 millimeters in inner channel length, 5.6 millimeters in outer channel length, 0.8 millimeters in innermost diameter, 2.6 millimeters in outermost diameter, 0.1 millimeters in catalyst layer thickness, and 0.2 millimeters in wall thickness. The spacing between the inner channel and the outer channel is 0.4 millimeters and remains constant. The continuous flow reactor can have any dimension unless restricted by design requirements. All the walls have the same thickness. One of the potential problems associated with the continuous flow reactor continues to be combustion stability. The maximum Reynolds number is less than 360 at the flow inlet and 960 when the velocity of the flow of the fluid is highest in the channels. The model is implemented in commercially available software FLUENT to obtain the solution of the problem. Detailed chemistry is included in the model. Detailed chemical mechanisms are playing an increasingly important role in developing chemical kinetics models for combustion. Detailed chemical mechanisms are incorporated into the reacting flow for the continuous flow reactor. The homogeneous combustion is modeled with the detailed chemical mechanism for methane oxidation in CHEMKIN format. Detailed heterogeneous chemistry in SURFACE-CHEMKIN format is included in the model.
Contributor: Junjie Chen, E-mail address: koncjj@gmail.com, ORCID: 0000-0002-5022-6863, Department of Energy and Power Engineering, School of Mechanical and Power Engineering, Henan Polytechnic University, 2000 Century Avenue, Jiaozuo, Henan, 454000, P.R. China
DOI: 10.17632/jmgng9dbc3.1
title: Health professions faculty's perception of teaching and learning during the COVID-19 pandemic

description: Data cleaning and analysis. Questionnaire design
DOI: 10.17632/h6ggsd3n6p.1
title: Metagenomics

description: Metagenomic raw data of different samples
DOI: 10.17632/j2cczbz58p.1
title: Carbon dioxide mole fraction data at different pressures pertaining to the heterogeneously catalyzed oxidation process in steam reforming reactor systems

description: The carbon dioxide mole fraction data at different pressures are obtained for the heterogeneously catalyzed oxidation process in steam reforming reactor systems. The reactor system is configured for simultaneous oxidation and steam reformation of methanol. The reactor system comprises two separate sets of flow channels, which are located between spaced, highly heat-conductive metal or ceramic separating walls. The medially located, bi-catalytic separating walls have different catalysts on opposed surfaces. These catalysts are selected for the particular reaction taking place in the adjacent reaction zone. The reactor provides for continuous and simultaneous reaction of two different process reaction streams in the channels defined between the walls, wherein a first process reaction stream undergoes a high temperature exothermic reaction in the first set of flow channels and a second process reaction stream undergoes an endothermic heat-consuming reaction in the second set of flow channels separated from the first set of flow channels by the heat transfer separating walls. More specifically, the reactor system includes a set of reforming channels for steam reformation of methanol and a set of oxidation channels for heating the reactor system to operating temperature. A separating wall therefore separates two adjacent reaction zones and also functions to transfer heat from the oxidation occurring at the catalyst surface in the oxidation zone directly to the reforming catalyst coated on the opposed surface. The channels are 0.7 millimeters in height and in width and 30.0 millimeters in length. To ensure the mechanical strength at elevated pressures, the thickness of the uncoated walls and the catalyst layers is 0.7 millimeters and 0.1 millimeters, respectively. The oxidation catalyst consists essentially of oxides of copper, zinc and aluminum. The reforming catalyst consists essentially of copper and oxides of zinc and aluminum. The exothermic and endothermic processes are conducted with a methanol-air equivalence ratio of 0.8 and a steam-to-methanol molar ratio of 1.17. The inlet temperature of the mixtures is 373 degrees kelvin. The gas velocity is 2.0 meters per second at the reforming channel inlets and 0.6 meters per second at the oxidation channel inlets, thereby assuring sufficient heat in the reactor. Heterogeneous reactions at a catalytically active surface affect the heat and mass balance at the surface. The heat release and consumption due to a surface reaction must be included in the model. Endothermicity or exothermicity of surface reactions contribute to the energy balance at an interface.
Contributor: Junjie Chen, E-mail address: koncjj@gmail.com, ORCID: 0000-0002-5022-6863, Department of Energy and Power Engineering, School of Mechanical and Power Engineering, Henan Polytechnic University, 2000 Century Avenue, Jiaozuo, Henan, 454000, P.R. China
DOI: 10.17632/d6kyhz8tb7.1
title: Metagenomics

description: Metagenomics raw data of different samples
DOI: 10.17632/njdgtskp38.1
title: Rapid Detection of Rice Striped Stem Borer（Chilo suppressalis Walker）Based on Terahertz Imaging and Spectrum

description: Terahertz Imaging and Spectrum
DOI: 10.17632/rxd4z2x67d.1
title: Qualitative dataset of stunting problem solving based on mothers needs

description: This data set is based on the results of coding, indexing and categorization of transcripts from a focused discussion group with several mothers who have children with stunting indications at the age of less than two years. This dataset was created using the Nvivo 12 software.
DOI: 10.17632/bsrkhh4h8f.1
title: Mo contents and Mo isotopes for the Early Jurassic mafic rocks

description: Mo contents and Mo isotopes for the Early Jurassic mafic rocks
DOI: 10.17632/278c6zx8c6.1
title: pMAD quantification

description: Contains .csv files that were generated from analyzing pMAD microscopy images using Imaris. Also contains R script for generating graphs for the width of pMAD domain and intensity profiles of each genotype.
DOI: 10.17632/mjwvjd5g7t.1
title: Volumetric flow rate data with different catalyst support porosity pertaining to the endothermic and exothermic chemical reactions in microchannel reactors

description: The volumetric flow rate data with different catalyst support porosity are presented for the endothermic and exothermic chemical reactions in in microchannel reactors. In physics and engineering, in particular fluid dynamics, the volumetric flow rate, also known as volume flow rate, or volume velocity, is the volume of fluid which passes per unit time. It contrasts with mass flow rate, which is the other main type of fluid flow rate. In most contexts a mention of rate of fluid flow is likely to refer to the volumetric rate. Volumetric flow rate should not be confused with volumetric flux, as defined by Darcy's law. The integration of a flux over an area gives the volumetric flow rate. The microchannel reactor provides for continuous and simultaneous reaction of two different process reaction streams in the channels defined between the walls, wherein a first process reaction stream undergoes a high temperature exothermic reaction in the first set of flow channels and a second process reaction stream undergoes an endothermic heat-consuming reaction in the second set of flow channels separated from the first set of flow channels by the heat transfer separating walls. More specifically, the microchannel reactor includes a set of reforming channels for steam reformation of methanol and a set of oxidation channels for heating the reactor system to operating temperature. A separating wall therefore separates two adjacent reaction zones and also functions to transfer heat from the oxidation occurring at the catalyst surface in the oxidation zone directly to the reforming catalyst coated on the opposed surface. The channels are 0.7 millimeters in height and in width and 30.0 millimeters in length. To ensure the mechanical strength at elevated pressures, the thickness of the uncoated walls and the catalyst layers is 0.7 millimeters and 0.1 millimeters, respectively. The oxidation catalyst consists essentially of oxides of copper, zinc and aluminum. The reforming catalyst consists essentially of copper and oxides of zinc and aluminum. The exothermic and endothermic processes are conducted with a methanol-air equivalence ratio of 0.8 and a steam-to-methanol molar ratio of 1.17. The inlet temperature of the mixtures is 373 degrees kelvin. The gas velocity is 2.0 meters per second at the reforming channel inlets and 0.6 meters per second at the oxidation channel inlets, thereby assuring sufficient heat in the reactor. ANSYS FLUENT is applied to the problem involving surface chemistry. ANSYS FLUENT handles thermodynamic properties, transport properties, equation-of-state, and chemical kinetics.
Contributor: Junjie Chen, E-mail address: koncjj@gmail.com, ORCID: 0000-0002-5022-6863, Department of Energy and Power Engineering, School of Mechanical and Power Engineering, Henan Polytechnic University, 2000 Century Avenue, Jiaozuo, Henan, 454000, P.R. China
DOI: 10.17632/jv9gpfbpjy.1
title: Live Imaging Tracking Scripts

description: R scripts used to process tracking data for extraction of transcriptional kinetics. Includes script used for creating a model of WT enhancer output based on the parameters extracted from individual enhancer deletions.
DOI: 10.17632/hzfbmj5hjt.1
title: pFES_data

description: Gait kinematic data for assesment of pFES therapeutic effect.
DOI: 10.17632/hzfbmj5hjt.2
title: pFES_data

description: Gait kinematic data for assesment of pFES therapeutic effect.
DOI: 10.17632/7ktscvmxvg.3
title: ComPara: A Corpus Linguistics Dataset of Computation in Architecture

description: A corpus linguistics built to study the language of computational architecture, or architecture which focuses on technology developments. The corpus includes: (1) the volume titles, titles of articles and introduction keywords for the journal Architectural Design (AD) to retrieve keynotes in theoretical discourse, and (2) titles and abstracts of winning and honourable mentions of the eVolo Skyscraper competition to retrieve words in conceptual project titles and their descriptions. This dataset has around 100.000 words and can serve as a basis for quantitative, qualitative or mixed method analysis of the language used in AD and the eVolo skyscraper competition between 2005 and 2019. As AD is recognized as one of the journals focusing on the 'digital turns' in architecture, and eVolo is a the most prestigious architecturalcompetition which It includes .txt and .csv files as well as .svg and wordclouds.