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RIM schemes | RI | Density (g/cm3) | Viscosity (mPa·s) | Techniques | Estimated cost (CNY/L) | Applications | References |
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64.8 wt% sodium iodide 35.2 wt% water | 1.491 at 26.7°C | 1.84 | 2.705 | LDA | 235.16 | Turbulent Taylor-Couette flow in an annulus | [37] |
64.49 wt% sodium iodide 35.51 wt% water | 1.490 | 1.88 | | PIV | 233.05 | Flow characteristics of simulated fast reactor fuel subassembly | [40] |
62-64 wt% sodium iodide 36-38 wt% water | 1.490-1.500 | 1.80 | 1.980 | PIV | 216.71-229.74 | Unsteady flow field within a two-stage axial turbomachine | [50] |
62-64 wt% sodium iodide 36-38 wt% water | 1.490-1.500 | 1.80 | 1.980 | PIV | 216.71-229.74 | Analysis of the flow field in the entire stage of an axial turbopump | [33] |
62-64 wt% sodium iodide 36-38 wt% water | 1.490-1.500 | 1.80 | 1.980 | PIV | 216.71-229.74 | Average passage flow field and deterministic stresses in the tip and hub regions of a multistage turbomachine | [51] |
62-64 wt% sodium iodide 36-38 wt% water | 1.490-1.500 | 1.80 | 1.980 | PIV | 216.71-229.74 | Analysis of the flow field in the entire stage of an axial turbopump | [52] |
62-64 wt% sodium iodide 36-38 wt% water | 1.490-1.500 | 1.80 | 1.980 | PIV | 216.71-229.74 | Flow nonuniformities and turbulent “hot spots” in a multistage turbomachine | [53] |
62-64 wt% sodium iodide 36-38 wt% water | 1.490-1.500 | 1.80 | 1.980 | PIV | 216.71-229.74 | Flow and turbulence within the wake and boundary layer of a rotor blade in a multistage turbomachine | [54] |
62-64 wt% sodium iodide 36-38 wt% water | 1.490-1.500 | 1.80 | 1.980 | PIV | 216.71-229.74 | Flow structure and turbulence caused by wake-blade and wake-wake interactions within a multistage turbomachine | [55] |
62-64 wt% sodium iodide 36-38 wt% water | 1.490-1.500 | 1.80 | 1.980 | PIV | 216.71-229.74 | Decomposition of the spatially filtered and ensemble averaged kinetic energy in a rotor wake | [56] |
62-64 wt% sodium iodide 36-38 wt% water | 1.490-1.500 | 1.80 | 1.980 | PIV | 216.71-229.74 | Turbulence within a multistage turbomachine rotor wake | [57] |
62-64 wt% sodium iodide 36-38 wt% water | 1.490 | 1.80 | 1.980 | Stereoscopic PIV | 216.71-229.74 | Turbulence within the tip-leakage vortex of an axial waterjet pump | [58] |
64 wt% sodium iodide 36 wt% water | 1.490 | | | PIV | 229.74 | Study on the flow field in a centrifugal pump | [59–61] |
64 wt% sodium iodide 36 wt% water | 1.490 | | | PIV | 229.74 | Frequency and scaling effects of jet interaction in a feedback-free fluidic oscillator | [62] |
63.3 wt% sodium iodide 36.7 wt% water | 1.489 | | | PIV | 225.10 | Gas-fluid flow inside a hydrocyclone with an air core | [63] |
63.0 wt% sodium iodide 37.0 wt% water | | 1.80 | ~1.980 | PIV | 223.14 | Vortical structures and turbulence statistics in the near wake of tabs with various geometries | [64] |
62.5 wt% sodium iodide 37.5 wt% water | 1.495 | | | PIV | 219.90 | Flow inside the model of an intake port of an automotive combustion engine | [65] |
62.932 wt% sodium iodide 36.968 wt% water 0.1 wt% sodium thiosulfate | 1.490 at 25°C | 1.867 | 2.603 | PIV | 259.87 | Flow characteristics in a 19-pin wire-wrapped fuel bundle | [66] |
62.5 wt% sodium iodide 36.5 wt% water 1 wt% sodium thiosulfate | 1.495 at 18°C | ~1.80 | ~1.980 | PIV | 219.90 | A versatile refractive-index-matched experimental facility for flow study | [67] |
61.6 wt% sodium iodide 38.4 wt% water | 1.485 | | | PIV | 214.19 | Flow structure and heat transfer characteristics for sphere-packed pipes | [68] |
61.6 wt% sodium iodide 38.4 wt% water | 1.485 | | | PIV | 214.19 | Complex flow structure in a three-dimensionally connected dual elbow | [69] |
61.5 wt% sodium iodide 38.5 wt% water | 1.490 | | | LDA | 213.56 | Flow field downstream spacer grids | [70] |
60.0 wt% sodium iodide 40.0 wt% water | ~1.500 | ~1.73 | ~2.387 | PIV | 204.35 | Flow field characteristics in single and dual S-shape 90° bends | [71] |
60 wt% sodium iodide 40 wt% water | ~1.500 | 1.73 | 2.387 | PIV | 204.35 | Internal jet interactions in a fluidic oscillator at low flow rate | [72] |
Sodium iodide Water | ~1.500 | | | PIV | 204.35 | Velocity and deformation in flows through compliant diaphragms | [73] |
Sodium iodide Water | 1.485 | | | PIV | 214.19 | Particle velocities in the rotating impeller of a slurry pump | [74] |
Sodium iodide Water | | | | LDA | 213.56 | Turbulent characteristics of the flow in an axially rotating pipe | [75] |
79 vol% sodium iodide 20 vol% glycerin 1 vol% water | 1.490 at 25°C | 1.75 | 6.650 | LDA | 213.56 | Mean flow velocity patterns within a ventricular assist device | [76] |
79 vol% sodium iodide 20 vol% glycerin 1 vol% water | 1.490 at 25°C | 1.75 | 6.650 | LDA | 213.56 | Mean velocity and Reynolds stress fields within an artificial heart ventricle | [77] |
79 vol% sodium iodide 20 vol% glycerin 1 vol% water | 1.490 at 25°C | 1.75 | 6.650 | Stereoscopic PIV | 213.56 | Effect of mitral valve orientation on three-dimensional flow in a left ventricle model | [78] |
74 vol% sodium iodide 21 vol% glycerin 5 vol% distilled water | 1.485 | 1.70 | 5.40 | Micro-PIV | 214.19 | Flow characterization through a network cell | [79] |
Sodium hydroxide Water | | | | Shadowgraphy PIV, two-tracer LIF | | Fluid dynamics and changes of PH in a bubble column | [80] |
p-Cymene | 1.491 | | | DPTV | 116.96 | Analysis of the flow field in a rod bundle | [81] |
p-Cymene | 1.490 | | | PTV | 116.96 | Movement of large dispersed beads in a vertical column | [82] |
p-Cymene | 1.490 | 0.860 | 1.020 | PTV | 116.96 | Pore geometry and fluid velocity in a bed of irregularly packed spheres | [83] |
p-Cymene | 1.490 | | | PTV | 116.96 | Flow velocity fields in a packed bed reactor | [84] |
p-Cymene | 1.490 | | | PIV | 116.96 | Flow visualization in a pebble bed reactor | [38] |
p-Cymene | 1.490 | | | PIV | 116.96 | Flow fields in a 61-pin wire-wrapped hexagonal fuel bundle | [85–87] |
p-Cymene | 1.490 | | | Time-resolved PIV | 116.96 | Flow characteristic in a facility of randomly packed spheres | [88] |
p-Cymene | 1.490 at 20°C | 0.855 | 0.810 | Time-resolved PIV | 116.96 | Time-resolved velocity measurements in a pipe of randomly packed spheres | [89] |
p-Cymene | 1.490 | | | PIV | 116.96 | Flow visualization in a model helical coil steam generator | [41, 90] |
p-Cymene | 1.490 | 0.860 | 1.02 | LDA stereoscopic PIV | 116.96 | Multiphase research on solid–liquid dispersion | [91] |
p-Cymene | 1.490 | 0.860 | 1.020 | Binocular camera | 116.96 | Influence of liquid motions on the dynamics of immersed pendulums | [92] |
p-Cymene | 1.490 | 0.860 | 1.020 | Laser sheet scan and CCD camera | 116.96 | Influence of aspect ratio on the distribution of porosity and velocity in columns of spheres | [93] |
p-Cymene | 1.490 | 0.860 | 1.020 | PTV | 116.96 | Velocity distribution of liquid in porous medium | [94] |
p-Cymene | 1.489 | 0.855 | 1.023 | PTV | 116.96 | Velocities and solid fraction in liquid-granular flows | [95] |
p-Cymene | 1.491 at 20°C | 0.860 | 0.833 | PIV | 116.96 | Turbulence characteristic in a high-throughput-stirred vessel | [96] |
p-Cymene | 1.488 | | | PIV, LIFT, DICs, and PT | 116.96 | Nuclear fuel assembly response to seismic loading | [97] |
p-Cymene | 1.490 at 20°C | 0.860 | 0.876 | LDA | 116.96 | Internal flow characteristic in scaled pressure-swirl atomizer | [98] |
p-Cymene | 1.490 | 0.855 | 0.810 | Time-resolved PIV | 116.96 | Velocity fields and characteristic in a 61-pin wire-wrapped bundle | [99] |
p-Cymene | 1.490 | 0.855 | 0.810 | Time-resolved PIV | 116.96 | Turbulent flow and vortex characteristics in a blocked subchannel of a wire-wrapped rod bundle | [100] |
p-Cymene | 1.490 | 0.855 | 0.810 | Time-resolved PIV | 116.96 | Cross flow mixing and streamwise vortex characteristics in a randomly packed bed | [101] |
99 vol% p-Cymene 1 vol% cinnamaldehyde | 1.492 | | | PLIF | 118.27 | Flow characteristic in a rod bundle | [102] |
98.4-99.2 vol% p-Cymene 0.8-1.6 vol% cinnamaldehyde | 1.490-1.494 | 0.859-0.860 | | PLIF | 118.01-119.06 | Proposed an RIM fluid scheme | [103] |
Dibutyl phthalate | 1.490 | ? | 15.0 | Optical probe | 22.92 | Vorticity distribution in the liquid flow | [104] |
Dibutyl phthalate | 1.490 at 25°C | 1.05 | 20.30 | PIV | 22.92 | Velocity field on the fluid-porous medium interface | [105] |
Dibutyl phthalate | 1.491 at 20°C | | 21.0 | LIF | 22.92 | Drainage displacement under combined capillary and gravity effects in porous media | [106] |
69.2 vol% turpentine 30.8 vol% tetraline | 1.489 at 25.15°C | 0.894 | 1.530 | LDA | 38.11 | Velocity characteristic of steady flows through engine inlet ports and cylinders | [35] |
68.2 vol% turpentine 31.8 vol% tetraline | 1.489 at 25.15°C | 0.894 | 1.46 | LDA | 38.18 | Particle motion and turbulence in dense two-phase flows | [107] |
68.2 vol% turpentine 31.8 vol% tetraline | 1.489 at 25.15°C | 0.894 | 1.458 | LDA | 38.18 | Particle velocities in a swirling, confined flow | [108] |
68.2 vol% turpentine 31.8 vol% tetraline | 1.489 at 25.15°C | 0.894 | 1.458 | LDA | 38.18 | Flow in the coolant passages of an internal combustion engine cylinder head | [34] |
62.9 vol% turpentine 37.1 vol% tetraline | 1.491 | 0.890 | 1.47 | LDA | 38.54 | Sedimentation and sediment flow in settling tanks with inclined walls | [109] |
72.2 vol% tetraline 27.8 vol% absolute alcohol | 1.490 at 25°C | 0.918 | 1.407 | | 32.47 | Purposed an RIM fluid scheme | [110] |
85 wt% Triton X-100 15 wt% water | 1.470 | 1.06 | 320 | PIV | 22.43 | Mobile granular layer in bedload transport by laminar-shearing flows | [111] |
Triton X-100 | 1.489 | 1.07 | 240 | LDA | 23.56 | Wall slip velocity coefficients in concentrated suspensions of noncolloidal particles | [112] |
Triton X-100 Zinc chloride Demineralized water | 1.491 | | at 23°C | Digital CCD camera | 158.84 | Full shear-induced self-diffusion tensor of noncolloidal suspensions | [113] |
77.93 wt% Triton X-100 9.01 wt% zinc chloride 13.06 wt% water | | | at 27°C | CCD color camera | 190.34 | Shear-induced radial segregation in the parallel-plate geometry | [114] |
76.2 wt% Triton X-100 14.35 wt% zinc chloride 9.31 wt% water 0.14 wt% hydrochloric acid | 1.491 | | | PIV PTV | 158.84 | Interaction of two small freely moving spheres in a linear flow field of yield stress fluids | [115] |
76 wt% Triton X-100 16.2 wt% zinc chloride 7.8 wt% water | 1.491 at 20°C | 1.18 | at 23°C | Time-lapse video record | 152.38 | Concentration band dynamics in free-surface Couette flow of a suspension | [116] |
50 vol% Triton X-100 23 vol% 1,6-dibromohexane 13.5 vol% UCON 75-H-90000 13.5 vol% UCON 75-H-450 | 1.4873 at 20°C | 1.18 | 480 at 20°C | LDA | 48.26 | Motion of concentrated suspensions in two-dimensional channel flow | [24, 25] |
77 wt% UCON 75-H-90000 23 wt% D.E.R331 liquid epoxy resin | 1.489 | | | PIV | 35.75 | Drop deformation and break-up in concentrated suspensions | [117] |
62 wt% UCON 50-HB-5100 38 wt% tetrabromoethane | 1.491 | | at 21.6 °C 1.72 ×103 at 29°C | Video recordings | 237.98 | Particle clusters in concentrated suspensions | [118] |
35.66 wt% UCON 75-H-90000 14.07 wt% TBE 50.27 wt% Triton X-100 0.014 wt% Tinuvin 328 | 1.491 | 1.18 | at 23.15°C | NMRI | 85.98 | Particle migration in Couette flow of concentrated suspensions | [119, 120] |
33.7 wt% UCON oil 24.4 wt% TBE 41.8 wt% terpineol 0.1 wt% Tinuvin | 1.491 | | | High-speed-digitized video system | 128.25 | Particle motions in concentrated suspensions | [121] |
62.2 wt% UCON oil 37.7 wt% TBE 0.1 wt% Tinuvin | 1.491 | | | High-speed-digitized video system | 173.29 | Solid particle dynamics in shear flow | [122] |
UCON oil TBE Triton X-100 0.3 wt% Tinuvin 328 | 1.491 | 1.18 | | LDA | 46.32 | Slow viscous flows of highly concentrated suspensions | [26, 27] |
Sunflower oil | 1.473 | | | LDA | 220.80 | Shear stresses and mixing in progressive flow regimes within annular-flow bioreactors | [22] |
Canola oil | 1.470 | | 43.0 | Shadow imaging PTV | 18.2 | Flow velocity in porous media | [123] |
65.6 vol% cyclohexyl bromide 34.4 vol% decalin | | | 2.06 | Confocal laser-scanning microscopy | 312.49 | Structure and dynamics of colloidal depletion gels | [30] |
74 wt% cyclohexyl bromide 26 wt% decalin | 1.490 | | | Camera | 323.92 | Particle dynamics and effective temperature of jammed granular matter in a slowly sheared three-dimensional | [124] |
Cyclohexyl bromide Decalin Tetrabutyl-ammonium chloride | ~1.490 | | | CARS microscopy | 308.15 | Repulsive and attractive colloidal glasses | [31] |
Cyclohexyl bromide Decalin Tetraline | 1.490 | | | Confocal fluorescence microscopy | 315.91 | Structure and dynamical heterogeneities near the colloid-gel transition | [28, 32] |
Decalin Tetraline Carbon tetrachloride | ~1.490 | | | Fluorescent confocal-scanning laser microscopy | 174.75 | Dynamical heterogeneities in colloidal hard-sphere suspensions | [29] |
85.5 vol% diethyl phthalate 14.5 vol% ethanol | 1.486 at 48.5°C | | | | 15.41 | Flow visualization in hydraulic cardiovascular models | [125] |
71 wt% potassium thiocyanate 29 wt% water | 1.491 | | | LDA | 13.10 | Axial flow field in stenosed carotid artery bifurcation models | [21] |
60.36 wt% ammonium thiocyanate 39.64 wt% water | | 1.13 | 2.06 | Stereoscopic PIV | 10.54 | Transitional and turbulent flow in a bed of spheres | [126] |
60.36 wt% ammonium thiocyanate 39.64 wt% water | | 1.13 | 2.06 | PIV | 10.54 | Transitional and turbulent flow in a bed of spheres | [127] |
Potassium thiocyanate Ammonium thiocyanate Water | | | | LDA | 13.10 | Steady flow in abdominal aortic aneurysm models | [20] |
Potassium thiocyanate Ammonium thiocyanate Glycerin | 1.490 | | | Videotape recording | 13.10 | Oscillatory flow in a model bifurcation | [128] |
Ammonium thiocyanate Glycerin Water | 1.485-1.488 | | 4.990 | | 26 | Purposed an RIM fluid scheme | [129] |
Glycerin | | | | PIV PTV PLIF | 26 | Flow and separation characteristic of concentrated liquid–liquid dispersions | [130] |
Glycerin Water | | | | Microfiber sensor | 15 | Proposed a waveguide device based on near infrared fingerprint spectrum | [131] |
Glycerin Water | | | | Hot film anemometer, LDA | 15 | Flow development in curved circular pipes | [132] |
45 vol% glycerin 55 vol% water | | | | Tomographic PIV | 12.26 | Airflow in disordered nasal cavity and its corrected models | [19] |
40.67 wt% glycerin 22.82 wt% ethylene glycol 36.51 wt% styrene glycol | | | 280 | Marked particle and stopwatch | 51.80 | Shear-induced self-diffusion in concentrated suspensions of spheres | [133] |
60 vol% glycerin 40 vol% water | 1.420 | ~1.10 | 1.10-1.38 | Digital in-line holography | 16.01 | Flow characterization in a lid-driven cylindrical cavity | [134] |
2,2-thiodiethanol Phosphate-buffered saline Glycerin | 1.489 at 22.25°C | 1.19 | | PIV | 75 | Purposed an RIM fluid scheme | [135] |
Glycerin Water | | 1.267 | 1500 | Three-dimensional flow visualization arrangement | 15 | Blob mechanics in flow through porous media | [136] |
60.82 wt% zinc iodide 39.18 wt% water | 1.494 at 21°C | | | Electromagnetic mirror scanner | 1728.23 | Internal flow of ink jet aspirators | [137] |
Hexadecane Microscope oil | | 0.890 | 25.0 | PIV | 1123.60 | Flow of a very concentrated slurry in a parallel-plate device | [138] |
Shellflex 214 BG oil Kerosene | ~1.490 | | 10.0 at 40 °C | LDA | | Steady entry flow in a curved pipe | [36] |
Kerosene | 1.440 | | | | 10 | Purposed an RIM fluid scheme | [139] |
8.9 wt% cassia oil 91.1 wt% castor oil | 1.489 | 0.970 | | PIV | 24.43 | Wall slip and slip layer thickness of hard-sphere suspensions | [140] |
61.5 wt% sucrose 38.5 wt% water | 1.446 | 1.30 | 79.0 | PIV PLIF | 20.20 20.81 | Mixing process of two miscible fluids in a lid-driven cavity | [141] |
66.5 wt% sucrose 8.87 wt% sodium chloride 24.63 wt% water | 1.481 at 25°C | 1.41 | 1.36 ×103 | PIV | 23.69 | Mechanisms for drawdown of floating particles in a laminar-stirred tank flow | [142] |
77.2 wt% maltose 22.8 wt% water | 1.487 at 21°C | 1.39 | | PIV | 209.17 | Flow fields under laminar conditions in two typical regions of a cavity transfer dynamic mixer | [143] |
Silicon fluid | 1.490 | 0.990 | 40.4 | Camera digital thermometer | 220 | Flow visualization and heat transfer in packed beds | [144] |
50 vol% Isane 50 vol% Marcol | | | | PIV | | Multiphase flow characterization in the nuclear fuel reprocessing | [145] |
Dow Corning 550 Dow Corning 200 | ~1.490 | | | Laser anemometer | 880.16 | Fluid velocity inside porous media | [146] |
83 wt% Dow Corning 550 17 wt% Dow Corning 556 | 1.489 at 19.8°C | | | Camera | 941.57 | Pore-scale flow and transport in porous media | [147] |
84 wt% Dow Corning 550 16 wt% Dow Corning 556 | 1.490 | 1.05 | 0.9975 | PLIF | 952.84 | Pore-scale flow and transport in porous media | [148] |
73 wt% Dow Corning 550 27 wt% Union Carbide L42 | 1.491 at 13.8°C | 1.06 at 25°C | | PIV | 831.52 | Flow measurement in porous media | [149] |
83 wt% Dow Corning 550 17 wt% Dow Corning 556 | 1.489 at 19.8 °C | | | PTV | 941.57 | Velocity fields and their volumetric averaging characteristic in porous media | [150] |
81.96 wt% Dow Corning 550 18.03 wt% Dow Corning 556 | 1.491 | 0.887 | 53.2 | TV camera | 930 | Flow visualization in single- and double-brush-sealing rings | [151] |
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