ライフサイエンスコーパス: boiling point

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

2 which deteriorate at temperatures above the boiling point.

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

4 id form even at temperatures exceeding their boiling points.

5 GC separates hydrocarbon molecules by boiling points.

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

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

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

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

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

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

12 Using calculated boiling points and characteristic mass spectral fragment

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

33 Boiling points derived from 1D separations were matched

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

49 .6 mus, and at 80 K, which is just above the boiling point of liquid nitrogen, they are respectively

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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