ライフサイエンスコーパス: boiling point

1 of a broader range of compounds in terms of boiling point.

2 various solvents with different polarity and boiling point.

3 properties such as enthalpy of formation and boiling point.

4 the 50-fold variation of viscosity up to the boiling point.

5 ich occurred only in systems poised near the boiling point.

6 which deteriorate at temperatures above the boiling point.

7 ions ranging from ambient up to close to the boiling point.

8 larities, molecular weights, and melting and boiling points.

9 id form even at temperatures exceeding their boiling points.

10 GC separates hydrocarbon molecules by boiling points.

11 bration spectroscopy, we show that, near its boiling point (~20 K), H(2) adsorbed on a well-ordered m

12 ompounds ranging from 80 to 238 degrees C in boiling point, (3) a mixture of five organic chemicals w

13 cessful modulation from n-pentane to pyrene (boiling points = 36/394 degrees C) is presented.

14 les were fried under vacuum (6.5 kPa, Twater-boiling-point=38 degrees C) or atmospheric conditions up

15 l driving force of 70 degrees C (Toil-Twater-boiling-point=70 degrees C).

16 rs that contain small volumes of liquid with boiling points a few degrees above body temperature.

17 Approximately below its boiling point, a significantly weak temperature dependen

18 Solution deposition using high-boiling-point additives such as octanedithiol (ODT) prov

19 In addition to boiling point, adsorbate structure and functionality aff

20 -B transesterification reaction, while lower boiling point alcohols such as MeOH and EtOH can replace

21 ily enter the gaseous state due to their low boiling point and high vapor pressure.

22 omatic hydrocarbons (PAHs), targeting normal boiling point and standard enthalpy of formation.

23 veal localized heating of silicon beyond its boiling point and suggest its subsequent phase explosion

24 olecules, which are known to have the lowest boiling point and the lowest intermolecular interactions

25 Using calculated boiling points and characteristic mass spectral fragment

26 and fatty acid methyl esters possessing high boiling points and low vapor pressures was performed usi

27 ative to wild type), almost reaching water's boiling point, and the highest increase with FRESCO to d

28 gree of overlap in compound vapor pressures, boiling points, and mass spectral fragmentation patterns

29 re, the hexylammonium molecules with a lower boiling point are selectively de-intercalated, which red

30 loring the use of viscous solvents with high boiling points as liquid matrices.

31 es between 8.3 x 10(-5) and 3.4 x 10(-3) and boiling points as low as -26.3 degrees C.

32 dibutyl ether with both low melting and high boiling points as the sole solvent.

33 emperature control allows organic gases with boiling points below 0 degrees C to be captured from air

34 improved the retention of volatiles with low boiling point (BP) (< 200 degrees C) and hydrophilic nat

35 asurement of total acid number (TAN) and TAN boiling point (BP) distribution for petroleum crude and

36 he second dimension separation (2DrelRT) and boiling point (BP).

37 is added and heated to temperatures close to boiling point, but little is released at temperatures <8

38 as methane, not only well above their normal boiling points, but also at relatively high temperatures

39 proton-transfer anion is strong enough that boiling points, but not melting points, may maximize at

40 er energy density (by 40 per cent), a higher boiling point (by 20 K), and is not soluble in water.

41 NDs with the higher boiling point C(4)F(10) vaporized at 1.15 MPa and emitte

42 correlation obtained by plotting theoretical boiling points calculated by COSMO-RS against experiment

43 m 1D separations were matched with predicted boiling points, calculated from the chemical structures

44 The "boiling point calibration" was successful as indicated b

45 ersely, the PCE of devices processed by high-boiling point chlorobenzene is less than 2%.

46 option for the storage of hydrogen near its boiling point, compared with adsorption at 77 K.

47 titive adsorption resulted in displacing low boiling point compounds by high boiling point compounds

48 splacing low boiling point compounds by high boiling point compounds during adsorption.

49 Among these, it is worth mentioning 5 high-boiling point compounds found in an olfactometric zone w

50 High boiling point compounds such as n-decane and 2,2-dimethy

51 uring thermal desorption prevents the higher-boiling-point compounds in the sample from reaching the

52 ag), retention behavior (Lee retention index/boiling point correlation, NIST Kovat's retention index)

53 kinetics revealed the importance of the low-boiling point cosolvent in removing oxygen prior to the

54 d, which enabled the characterization of its boiling point, density, refractive index, and its polari

55 rapid (<3 s) crystallization after a solvent boiling point-dependent film thinning transition, (ii) s

56 Boiling points derived from 1D separations were matched

57 ty and the boiling-point resolution (minimum boiling-point difference required for the separation of

58 the use of structure-property correlations, boiling point distributions of TAN values can be calcula

59 t the water-NAPL interface, which lowers the boiling point due to combined vapor pressures, potential

60 For DeltapK(a) values above 10, the boiling point elevation becomes so high (>300 degrees C)

61 f the dense liquid: For systems far from the boiling point, enzymes acted only on the droplet surface

62 Low-boiling-point FAs and PGA can be recycled through simple

63 , distillation temperature (T50%), and final boiling point (FBP) of commercial gasoline.

64 inary mixtures, and accurately predicted the boiling point, flash point, vapor pressure, and viscosit

65 ly reflecting the actual distribution of oil boiling point fractions (the hydrocarbon block profile)

66 ounds were present mainly in the mid to high boiling point fractions of the oils (C(14)-C(32) alkane

67 HF and dioxane can be heated way above their boiling point in sealed vessels using a small quantity o

68 ties for DR3TBDTT and PC71 BM, and different boiling points, is used for solvent vapor annealing (SVA

69 corresponding to a carbon number of 12 or a boiling point less than 200 degrees C in the permeate.

70 ess (Fc = ferrocene) as a model system, high boiling point (low vapor pressure) solvents give rise to

71 scribe a method for the stabilization of low-boiling point (low-bp) perfluorocarbons (PFCs) at physio

72 to alkanes, explaining their relatively low boiling points, low surface tensions, and poor solvent p

73 precursors onto activated carbon from a low-boiling-point, low-polarity solvent, such as acetone, re

74 ts of five to seven volatile test compounds (boiling point </=174 degrees C), the effects of the mini

75 ls containing C, H, F, Cl, Br, and I, having boiling points </=402 degrees C.

76 ed via a sol-gel process using nontoxic, low boiling point mixed solvents.

77 ize the sulfur are therefore limited to high-boiling-point monomers only.

78 n regarding the influence on its melting and boiling point (MP/BP).

79 with a low T(g) of -128 degrees C and a high boiling point of +145 degrees C enables stable energy st

80 When the growth reaction was above the boiling point of an amine ligand, the surface ligand dyn

81 Using GC retention times, the boiling point of CH(3)SeSSCH(3) was estimated to be appr

82 kerogen and show that kerogen suppresses the boiling point of decane due to the effect of confinement

83 gy gaps opening at temperatures close to the boiling point of liquid nitrogen (77 kelvin), which is a

84 .6 mus, and at 80 K, which is just above the boiling point of liquid nitrogen, they are respectively

85 ransition temperatures remain well below the boiling point of liquid nitrogen.

86 ing nanoporous adsorbents operating near the boiling point of methane (112 K), which is accessible th

87 are held at temperatures above and below the boiling point of the liquid, respectively.

88 erally correlate with the polarizability and boiling point of the refrigerant, with dichlorodifluorom

89 mely stable upon thermal treatment up to the boiling point of the solvent (about 300 degrees C), whic

90 linearly from 20 degrees C to 100 degrees C (boiling point of water).

91 erately elevated temperatures just above the boiling point of water, this chemistry has all the requi

92 the solution thermal denaturation beyond the boiling point of water.

93 supported by the monotonic dependence of the boiling points of n-alkanes on the chain length.

94 Solvents (COSMO-RS) was used to predict the boiling points of several polybrominated diphenyl ethers

95 intensive distillation due to the very close boiling points of ST and EB.

96 as dependent on the DART temperature and the boiling points of the analyte and matrix.

97 e pyrometer output voltage against the known boiling points of these solutions.

98 xact relation between GC retention times and boiling points of this and other Group VI B analogues (S

99 DeltaG(form)) of the metal chlorides and the boiling points of those metal chlorides.

100 were used: the first one consisted of a high boiling point oil (hexadecane), whereas the second was l

101 e), whereas the second was loaded with a low boiling point oil (perfluoropentane).

102 of chemically exfoliated MoS2 sheets in high boiling point organic solvents enabled by surface functi

103 Low-boiling point perfluorocarbon nanodroplets (NDs) are val

104 oplet surface, while systems poised near the boiling point permitted enzyme penetration.

105 lable, different physicochemical properties (boiling point, polarity, viscosity) could be exploited t

106 and retention time prediction from estimated boiling points predicted using molecular formulas and re

107 The collective use of boiling points predicted with COSMO-RS, and characterist

108 e component is demonstrated using these high boiling point processing additives.

109 perature programming is demonstrated for the boiling point range from n-C5 to n-C12.

110 roduced in a 37-s long separation spanning a boiling-point range from n-C10 (174 degrees C) to n-C28

111 (35 degrees C/min) was demonstrated for the boiling-point range from n-C5 to n-C44 (ASTM D2887 simul

112 e tetrabutylammonium molecules with a higher boiling point remain to support and stabilize the superl

113 production, the total peak capacity, and the boiling point resolution are determined for C10-C28 n-al

114 nhanced, but the total peak capacity and the boiling-point resolution (minimum boiling-point differen

115 en and helium at temperatures close to their boiling points shows, in some cases, unusually high mono

116 spheric pressure, the vent-water is close to boiling point so can entropically destabilize biomacromo

117 l molecule-polymer ratio), and additive high boiling point solvent concentrations on film fidelity, p

118 treatment with the low surface tension, low boiling point solvent dimethyl ether (DME).

119 llular fabrication method that drives a high boiling point solvent into the core of a block copolymer

120 e of a surface-stabilizing ligand and a high boiling point solvent to yield MoC(1-x) NPs that are col

121 e (DMSO) to demonstrate a reaction in a high boiling point solvent, and (iii) tryptic digestions of c

122 nt exchange (especially high-boiling- to low-boiling-point solvent), and catalyst separation.

123 rbons (HFCs, e.g., CH(3)CF(3)) to the higher-boiling point solvents (such as CH(3)Cl(3) and CCl(2)=CC

124 g electrolytes (e.g., ionic liquids) or high boiling point solvents to avoid complications associated

125 solution-phase synthesis, conducted in high boiling point solvents.

126 1) poor colloidal stability, 2) use of high-boiling-point solvents for QD dispersion, and 3) limitat

127 ible electrochemistry, whereas volatile (low boiling point) solvents need to be mixed with suitable l

128 ution of the total acid number (TAN) in true boiling point (TBP) distillation cuts from crude oil.

129 y of the fullerene component and (ii) higher boiling point than the host solvent.

130 negatively, and volatile thiols with higher boiling points that contribute positively to the aroma p

131 Below the boiling point, the effect of MWs on the activation energ

132 ral trends in their properties-for instance, boiling point trends as size increases.

133 high energy cost due to its low density and boiling point, which drives a high price.

134 ticomponent gas mixture with a wide range of boiling points with high reproducibility.