Review Article

Review of Refractive Index-Matching Techniques of Polymethyl Methacrylate in Flow Field Visualization Experiments

Table 1

Comparison of different RIM fluid schemes of PMMA.

RIM schemesRIDensity (g/cm3)Viscosity (mPa·s)TechniquesEstimated cost (CNY/L)ApplicationsReferences

64.8 wt% sodium iodide
35.2 wt% water
1.491 at 26.7°C1.842.705LDA235.16Turbulent Taylor-Couette flow in an annulus[37]
64.49 wt% sodium iodide
35.51 wt% water
1.4901.88PIV233.05Flow characteristics of simulated fast reactor fuel subassembly[40]
62-64 wt% sodium iodide
36-38 wt% water
1.490-1.5001.801.980PIV216.71-229.74Unsteady flow field within a two-stage axial turbomachine[50]
62-64 wt% sodium iodide
36-38 wt% water
1.490-1.5001.801.980PIV216.71-229.74Analysis of the flow field in the entire stage of an axial turbopump[33]
62-64 wt% sodium iodide
36-38 wt% water
1.490-1.5001.801.980PIV216.71-229.74Average 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
1.490-1.5001.801.980PIV216.71-229.74Analysis of the flow field in the entire stage of an axial turbopump[52]
62-64 wt% sodium iodide
36-38 wt% water
1.490-1.5001.801.980PIV216.71-229.74Flow nonuniformities and turbulent “hot spots” in a multistage turbomachine[53]
62-64 wt% sodium iodide
36-38 wt% water
1.490-1.5001.801.980PIV216.71-229.74Flow 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
1.490-1.5001.801.980PIV216.71-229.74Flow 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
1.490-1.5001.801.980PIV216.71-229.74Decomposition of the spatially filtered and ensemble averaged kinetic energy in a rotor wake[56]
62-64 wt% sodium iodide
36-38 wt% water
1.490-1.5001.801.980PIV216.71-229.74Turbulence within a multistage turbomachine rotor wake[57]
62-64 wt% sodium iodide
36-38 wt% water
1.4901.801.980Stereoscopic PIV216.71-229.74Turbulence within the tip-leakage vortex of an axial waterjet pump[58]
64 wt% sodium iodide
36 wt% water
1.490PIV229.74Study on the flow field in a centrifugal pump[5961]
64 wt% sodium iodide
36 wt% water
1.490PIV229.74Frequency and scaling effects of jet interaction in a feedback-free fluidic oscillator[62]
63.3 wt% sodium iodide
36.7 wt% water
1.489PIV225.10Gas-fluid flow inside a hydrocyclone with an air core[63]
63.0 wt% sodium iodide
37.0 wt% water
1.80~1.980PIV223.14Vortical structures and turbulence statistics in the near wake of tabs with various geometries[64]
62.5 wt% sodium iodide
37.5 wt% water
1.495PIV219.90Flow 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°C1.8672.603PIV259.87Flow 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~1.80~1.980PIV219.90A versatile refractive-index-matched experimental facility for flow study[67]
61.6 wt% sodium iodide
38.4 wt% water
1.485PIV214.19Flow structure and heat transfer characteristics for sphere-packed pipes[68]
61.6 wt% sodium iodide
38.4 wt% water
1.485PIV214.19Complex flow structure in a three-dimensionally connected dual elbow[69]
61.5 wt% sodium iodide
38.5 wt% water
1.490LDA213.56Flow field downstream spacer grids[70]
60.0 wt% sodium iodide
40.0 wt% water
~1.500~1.73~2.387PIV204.35Flow field characteristics in single and dual S-shape 90° bends[71]
60 wt% sodium iodide
40 wt% water
~1.5001.732.387PIV204.35Internal jet interactions in a fluidic oscillator at low flow rate[72]
Sodium iodide
Water
~1.500PIV204.35Velocity and deformation in flows through compliant diaphragms[73]
Sodium iodide
Water
1.485PIV214.19Particle velocities in the rotating impeller of a slurry pump[74]
Sodium iodide
Water
LDA213.56Turbulent characteristics of the flow in an axially rotating pipe[75]
79 vol% sodium iodide
20 vol% glycerin
1 vol% water
1.490 at 25°C1.756.650LDA213.56Mean flow velocity patterns within a ventricular assist device[76]
79 vol% sodium iodide
20 vol% glycerin
1 vol% water
1.490 at 25°C1.756.650LDA213.56Mean 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°C1.756.650Stereoscopic PIV213.56Effect 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
1.4851.705.40Micro-PIV214.19Flow characterization through a network cell[79]
Sodium hydroxide
Water
Shadowgraphy PIV, two-tracer LIFFluid dynamics and changes of PH in a bubble column[80]
p-Cymene1.491DPTV116.96Analysis of the flow field in a rod bundle[81]
p-Cymene1.490PTV116.96Movement of large dispersed beads in a vertical column[82]
p-Cymene1.4900.8601.020PTV116.96Pore geometry and fluid velocity in a bed of irregularly packed spheres[83]
p-Cymene1.490PTV116.96Flow velocity fields in a packed bed reactor[84]
p-Cymene1.490PIV116.96Flow visualization in a pebble bed reactor[38]
p-Cymene1.490PIV116.96Flow fields in a 61-pin wire-wrapped hexagonal fuel bundle[8587]
p-Cymene1.490Time-resolved PIV116.96Flow characteristic in a facility of randomly packed spheres[88]
p-Cymene1.490 at 20°C0.8550.810Time-resolved PIV116.96Time-resolved velocity measurements in a pipe of randomly packed spheres[89]
p-Cymene1.490PIV116.96Flow visualization in a model helical coil steam generator[41, 90]
p-Cymene1.4900.8601.02LDA stereoscopic PIV116.96Multiphase research on solid–liquid dispersion[91]
p-Cymene1.4900.8601.020Binocular camera116.96Influence of liquid motions on the dynamics of immersed pendulums[92]
p-Cymene1.4900.8601.020Laser sheet scan and CCD camera116.96Influence of aspect ratio on the distribution of porosity and velocity in columns of spheres[93]
p-Cymene1.4900.8601.020PTV116.96Velocity distribution of liquid in porous medium[94]
p-Cymene1.4890.8551.023PTV116.96Velocities and solid fraction in liquid-granular flows[95]
p-Cymene1.491 at 20°C0.8600.833PIV116.96Turbulence characteristic in a high-throughput-stirred vessel[96]
p-Cymene1.488PIV, LIFT, DICs, and PT116.96Nuclear fuel assembly response to seismic loading[97]
p-Cymene1.490 at 20°C0.8600.876LDA116.96Internal flow characteristic in scaled pressure-swirl atomizer[98]
p-Cymene1.4900.8550.810Time-resolved PIV116.96Velocity fields and characteristic in a 61-pin wire-wrapped bundle[99]
p-Cymene1.4900.8550.810Time-resolved PIV116.96Turbulent flow and vortex characteristics in a blocked subchannel of a wire-wrapped rod bundle[100]
p-Cymene1.4900.8550.810Time-resolved PIV116.96Cross flow mixing and streamwise vortex characteristics in a randomly packed bed[101]
99 vol% p-Cymene
1 vol% cinnamaldehyde
1.492PLIF118.27Flow characteristic in a rod bundle[102]
98.4-99.2 vol% p-Cymene
0.8-1.6 vol% cinnamaldehyde
1.490-1.4940.859-0.860PLIF118.01-119.06Proposed an RIM fluid scheme[103]
Dibutyl phthalate1.490?15.0Optical probe22.92Vorticity distribution in the liquid flow[104]
Dibutyl phthalate1.490 at 25°C1.0520.30PIV22.92Velocity field on the fluid-porous medium interface[105]
Dibutyl phthalate1.491 at 20°C21.0LIF22.92Drainage displacement under combined capillary and gravity effects in porous media[106]
69.2 vol% turpentine
30.8 vol% tetraline
1.489 at 25.15°C0.8941.530LDA38.11Velocity characteristic of steady flows through engine inlet ports and cylinders[35]
68.2 vol% turpentine
31.8 vol% tetraline
1.489 at 25.15°C0.8941.46LDA38.18Particle motion and turbulence in dense two-phase flows[107]
68.2 vol% turpentine
31.8 vol% tetraline
1.489 at 25.15°C0.8941.458LDA38.18Particle velocities in a swirling, confined flow[108]
68.2 vol% turpentine
31.8 vol% tetraline
1.489 at 25.15°C0.8941.458LDA38.18Flow in the coolant passages of an internal combustion engine cylinder head[34]
62.9 vol% turpentine
37.1 vol% tetraline
1.4910.8901.47LDA38.54Sedimentation and sediment flow in settling tanks with inclined walls[109]
72.2 vol% tetraline
27.8 vol% absolute alcohol
1.490 at 25°C0.9181.40732.47Purposed an RIM fluid scheme[110]
85 wt% Triton X-100
15 wt% water
1.4701.06320PIV22.43Mobile granular layer in bedload transport by laminar-shearing flows[111]
Triton X-1001.4891.07240LDA23.56Wall slip velocity coefficients in concentrated suspensions of noncolloidal particles[112]
Triton X-100
Zinc chloride
Demineralized water
1.491 at 23°CDigital CCD camera158.84Full 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°CCCD color camera190.34Shear-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
1.491PIV
PTV
158.84Interaction 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°C1.18 at 23°CTime-lapse video record152.38Concentration 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°C1.18480 at 20°CLDA48.26Motion of concentrated suspensions in two-dimensional channel flow[24, 25]
77 wt% UCON 75-H-90000
23 wt% D.E.R331 liquid epoxy resin
1.489PIV35.75Drop 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 recordings237.98Particle 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
1.4911.18 at 23.15°CNMRI85.98Particle 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
1.491High-speed-digitized video system128.25Particle motions in concentrated suspensions[121]
62.2 wt% UCON oil
37.7 wt% TBE
0.1 wt% Tinuvin
1.491High-speed-digitized video system173.29Solid particle dynamics in shear flow[122]
UCON oil
TBE
Triton X-100
0.3 wt% Tinuvin 328
1.4911.18LDA46.32Slow viscous flows of highly concentrated suspensions[26, 27]
Sunflower oil1.473LDA220.80Shear stresses and mixing in progressive flow regimes within annular-flow bioreactors[22]
Canola oil1.47043.0Shadow imaging
PTV
18.2Flow velocity in porous media[123]
65.6 vol% cyclohexyl bromide
34.4 vol% decalin
2.06Confocal laser-scanning microscopy312.49Structure and dynamics of colloidal depletion gels[30]
74 wt% cyclohexyl bromide
26 wt% decalin
1.490Camera323.92Particle dynamics and effective temperature of jammed granular matter in a slowly sheared three-dimensional[124]
Cyclohexyl bromide
Decalin
Tetrabutyl-ammonium chloride
~1.490CARS microscopy308.15Repulsive and attractive colloidal glasses[31]
Cyclohexyl bromide
Decalin
Tetraline
1.490Confocal fluorescence microscopy315.91Structure and dynamical heterogeneities near the colloid-gel transition[28, 32]
Decalin
Tetraline
Carbon tetrachloride
~1.490Fluorescent confocal-scanning laser microscopy174.75Dynamical heterogeneities in colloidal hard-sphere suspensions[29]
85.5 vol% diethyl phthalate
14.5 vol% ethanol
1.486 at 48.5°C15.41Flow visualization in hydraulic cardiovascular models[125]
71 wt% potassium thiocyanate
29 wt% water
1.491LDA13.10Axial flow field in stenosed carotid artery bifurcation models[21]
60.36 wt% ammonium thiocyanate
39.64 wt% water
1.132.06Stereoscopic PIV10.54Transitional and turbulent flow in a bed of spheres[126]
60.36 wt% ammonium thiocyanate
39.64 wt% water
1.132.06PIV10.54Transitional and turbulent flow in a bed of spheres[127]
Potassium thiocyanate
Ammonium thiocyanate
Water
LDA13.10Steady flow in abdominal aortic aneurysm models[20]
Potassium thiocyanate
Ammonium thiocyanate
Glycerin
1.490Videotape recording13.10Oscillatory flow in a model bifurcation[128]
Ammonium thiocyanate
Glycerin
Water
1.485-1.4884.99026Purposed an RIM fluid scheme[129]
GlycerinPIV
PTV
PLIF
26Flow and separation characteristic of concentrated liquid–liquid dispersions[130]
Glycerin
Water
Microfiber sensor15Proposed a waveguide device based on near infrared fingerprint spectrum[131]
Glycerin
Water
Hot film anemometer, LDA15Flow development in curved circular pipes[132]
45 vol% glycerin
55 vol% water
Tomographic PIV12.26Airflow in disordered nasal cavity and its corrected models[19]
40.67 wt% glycerin
22.82 wt% ethylene glycol
36.51 wt% styrene glycol
280Marked particle and stopwatch51.80Shear-induced self-diffusion in concentrated suspensions of spheres[133]
60 vol% glycerin
40 vol% water
1.420~1.101.10-1.38Digital in-line holography16.01Flow characterization in a lid-driven cylindrical cavity[134]
2,2-thiodiethanol
Phosphate-buffered saline
Glycerin
1.489 at 22.25°C1.19PIV75Purposed an RIM fluid scheme[135]
Glycerin
Water
1.2671500Three-dimensional flow visualization arrangement15Blob mechanics in flow through porous media[136]
60.82 wt% zinc iodide
39.18 wt% water
1.494 at 21°CElectromagnetic mirror scanner1728.23Internal flow of ink jet aspirators[137]
Hexadecane
Microscope oil
0.89025.0PIV1123.60Flow of a very concentrated slurry in a parallel-plate device[138]
Shellflex 214 BG oil
Kerosene
~1.49010.0 at 40 °CLDASteady entry flow in a curved pipe[36]
Kerosene1.44010Purposed an RIM fluid scheme[139]
8.9 wt% cassia oil
91.1 wt% castor oil
1.4890.970PIV24.43Wall slip and slip layer thickness of hard-sphere suspensions[140]
61.5 wt% sucrose
38.5 wt% water
1.4461.3079.0PIV
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°C1.411.36 ×103PIV23.69Mechanisms for drawdown of floating particles in a laminar-stirred tank flow[142]
77.2 wt% maltose
22.8 wt% water
1.487 at 21°C1.39PIV209.17Flow fields under laminar conditions in two typical regions of a cavity transfer dynamic mixer[143]
Silicon fluid1.4900.99040.4Camera digital thermometer220Flow visualization and heat transfer in packed beds[144]
50 vol% Isane
50 vol% Marcol
PIVMultiphase flow characterization in the nuclear fuel reprocessing[145]
Dow Corning 550
Dow Corning 200
~1.490Laser anemometer880.16Fluid velocity inside porous media[146]
83 wt% Dow Corning 550
17 wt% Dow Corning 556
1.489 at 19.8°CCamera941.57Pore-scale flow and transport in porous media[147]
84 wt% Dow Corning 550
16 wt% Dow Corning 556
1.4901.050.9975PLIF952.84Pore-scale flow and transport in porous media[148]
73 wt% Dow Corning 550
27 wt% Union Carbide L42
1.491 at 13.8°C1.06 at 25°CPIV831.52Flow measurement in porous media[149]
83 wt% Dow Corning 550
17 wt% Dow Corning 556
1.489 at 19.8 °CPTV941.57Velocity fields and their volumetric averaging characteristic in porous media[150]
81.96 wt% Dow Corning 550
18.03 wt% Dow Corning 556
1.4910.88753.2TV camera930Flow visualization in single- and double-brush-sealing rings[151]