162 results on '"Coquelet, C."'
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2. Red light violations by adult pedestrians and other safety-related behaviors at signalized crosswalks
3. Simulations of the Impact of Co-injected Gases on CO2 Storage, the SIGARRR Project: First Results on Water-gas Interactions Modeling
4. Equipment using a “static-analytic” method for solubility measurements in potentially hazardous binary mixtures under cryogenic temperatures
5. Solubility of ethylbenzene and xylene in pure water and aqueous alkanolamine solutions
6. Solubility data for toluene in various aqueous alkanolamine solutions
7. Vapor–Liquid Equilibrium Data for the Sulfur Dioxide (SO2) + Difluoromethane (R32) System at Temperatures from 288.07 to 403.16 K and at Pressures up to 7.31 MPa
8. Development of a New Alpha Function for the Peng–Robinson Equation of State: Comparative Study of Alpha Function Models for Pure Gases (Natural Gas Components) and Water-Gas Systems
9. Measurement of physical properties of refrigerant mixtures. Determination of phase diagrams
10. Solubility of hydrogen in methanol at temperatures from 248.41 to 308.20 K
11. Chiral macrocycles, part I: Synthesis and enantioselective transport of carboxylic acids as their Li+ salts
12. Representation of Solid, Liquid, and Vapor phases of Binary Lennard Jones Mixtures using the SLV-EoS
13. Vapor-liquid equilibrium data concerning refrigerant systems (R3110+R365mfc)
14. Experimental determination of liquid-liquid equilibrium data and their representation using the UNIQUAC and NRTL equations
15. Vapour–liquid equilibrium data for the difluoromethane+1,1,1,2,3,3,3-heptafluoropropane system at temperatures from 283.20 to 343.38 K and pressures up to 4.5 MPa
16. Investigation of the thermophysical properties of binary system CO 2 and Hydro-fluoro-olefins
17. Phase Equilibrium Properties Aspects of CO2and Acid Gases Transportation
18. Experimental Determination of the Solid- Liquid-Vapor Locus for the CH4-CO2-H2S System and Application to the Design of a New Low-Temperature Distillation Process for the Purification of Natural Gas
19. A NEW APPARATUS FOR THE COMPLETE DETERMINATION OF PHASE EQUILIBRIUM DATA FROM 0.05 – 10 bar
20. Liquid density and bubble pressure measurements for propylene + 2-propanol system
21. Performance of large pixelised Micromegas detectors in the COMPASS environment
22. New pixelized Micromegas detector with low discharge rate for the COMPASS experiment
23. Isothermal Vapor–Liquid Equilibrium Data for the Propan-1-ol + Dodecane System at (323.0, 343.4, 353.2, 363.1, and 369.2) K
24. Vapor−Liquid Equilibrium Data for Binary Systems Consisting of Either Hexafluoropropene (HFP) or 2,2,3-Trifluoro-3-(trifluoromethyl)oxirane (HFPO) with Carbon Dioxide (R-744) or 2,2-Dichloro-1,1,1-trifluoroethane (R-123)
25. Architecture and Implementation of the Front-End Electronics of the Time Projection Chambers in the T2K Experiment
26. Comparison of Different Options for Transmutation Scenarios Studied in the Frame of the French Law for Waste Management
27. Architecture and implementation of the front-end electronics of the time projection chambers in the T2K experiment
28. Isothermal P, x, y data for the argon+carbon dioxide system at six temperatures from 233.32 to 299.21K and pressures up to 14MPa
29. Solubility data for benzene in aqueous solutions of methyldiethanolamine (MDEA) and of diglycolamine (DGA)
30. Corrigendum to “Revised solubility data and modeling of water in the gas phase of the methane/water binary system at temperatures from 283.08 to 318.12 K and pressures up to 34.5 MPa”
31. Vapor–liquid equilibrium data for the sulfur dioxide (SO2) + 1,1,1,2,3,3,3-heptafluoropropane (R227ea) system at temperatures from 288.07 to 403.19 K and pressures up to 5.38 MPa
32. Vapour–liquid equilibrium measurements and correlation of the difluoromethane (R32) + propane (R290) + 1,1,1,2,3,3,3-heptafluoropropane (R227ea) ternary mixture at temperatures from 269.85 to 328.35K
33. Vapor–liquid equilibrium data for the carbon dioxide (CO2) + difluoromethane (R32) system at temperatures from 283.12 to 343.25 K and pressures up to 7.46 MPa
34. Solubility measurement and modeling of water in the gas phase of the methane/water binary system at temperatures from 283.08 to 318.12K and pressures up to 34.5MPa
35. Vapor–liquid equilibrium data for the CO2 + 1,1,1,2,3,3,3,-heptafluoropropane (R227ea) system at temperatures from 276.01 to 367.30 K and pressures up to 7.4 MPa
36. Vapor–liquid equilibrium data for the propane+1,1,1,2,3,3,3-heptafluoropropane (R227ea) system at temperatures from 293.16 to 353.18 K and pressures up to 3.4 MPa
37. La cochenille blanche du mûrier, principal ravageur des cassissiers en Région Rhône-Alpes
38. Catalase-like activity of a water-soluble complex of Ru(II)
39. Association between benzalkonium chloride and a poly( acrylic acid) gel. Study by microfiltration and membrane dialysis
40. Synthesis and complexation of macrocycles containing two pyrazolone sub-units
41. P 122 Retinoid effects on rabbit corneal glycocalyx synthesis in vitro
42. P 120 Determination of the tear volume as a method of assessing the precorneal residence time of various polymer formulations in rabbits
43. P 325 Effect of carteolol on the cytoskeleton and the phagocytosis capacity of cultured trabecular cells
44. Insulin-like growth factor-1 (IGF-1) specifically binds to bovine lens epithelial cells and increases the number of fibronectin receptor sites
45. Inhibition of Cell Adhesion to Lens Capsule by LCM 1910, an RGD-Derived Peptide
46. Qualitative analysis of pedestrians' perception of the urban environment when crossing streets.
47. Ocular anti-inflammatory activity of CBS-113 A, a dual inhibitor of cyclooxygenase and 5-lipoxygenase
48. ChemInform Abstract: New Unsymmetrical Tetradentate Macrocycles with sp3 and sp2 Nitrogen Donor Site‐Synthesis and Ru(II) Complexation.
49. Vapor−Liquid Equilibrium Data for Binary Systems Consisting of Either Hexafluoropropene (HFP) or 2,2,3-Trifluoro-3-(trifluoromethyl)oxirane (HFPO) with Carbon Dioxide (R-744) or 2,2-Dichloro-1,1,1-trifluoroethane (R-123).
50. Corrigendum to “Revised solubility data and modeling of water in the gas phase of the methane/water binary system at temperatures from 283.08 to 318.12K and pressures up to 34.5MPa”: [Fluid Phase Equilibria 214 (2003) 101–117]
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