DIN 51562-3-1985 Viscometry determination of kinematic viscosity using the Ubbelohde viscometer viscosity relative increment at short flow times《粘度测定法 用Ubberlohde粘度计测量动粘滞度 在短流动时间内相.pdf
《DIN 51562-3-1985 Viscometry determination of kinematic viscosity using the Ubbelohde viscometer viscosity relative increment at short flow times《粘度测定法 用Ubberlohde粘度计测量动粘滞度 在短流动时间内相.pdf》由会员分享,可在线阅读,更多相关《DIN 51562-3-1985 Viscometry determination of kinematic viscosity using the Ubbelohde viscometer viscosity relative increment at short flow times《粘度测定法 用Ubberlohde粘度计测量动粘滞度 在短流动时间内相.pdf(5页珍藏版)》请在麦多课文档分享上搜索。
1、Viscometry Determination of kinematic viscosity using the Ubbelohde viscometer Viscosity relative increment at short flow times 1 Scope and field of application DIN 51 562 Part 1 specifies a minimum flow time of 200 s for the volume between the filling marks, as in almost all standards dealing with
2、capillary viscometers. Even greater flow times are specified for cases where the Hagenbach correction at 200 s is not negligibly small. The specification of minimum flow times leads to difficulties in fields where short flow times have in practice been customary and required. When frequent measureme
3、nts are made in practice, flow times for pure solvents of above 200 s are too long, especially when determining the Staudinger function (viscosity number, see clause 2) of polymer solutions (e.g. in accordance with the DIN 53 728 standard series), since the flow times of the solutions are even highe
4、r and, additionally, there are difficulties in the handling of the capillaries. Experience has shown that for such measurements it is better to operate with wider capillaries and shorter flow times. This standard specifies a method of determining and applying the Hagenbach correction, which is essen
5、tial at low viscosities and short flow times, and offers, together with experimental instructions, a uniform working base. oiN 51 562 Part 3 2 Concepts (see also DIN 1342) The viscosity relative increment is defined by where q is the viscosity of the solution; qs is the viscosity of the solvent; qr
6、is the viscosity ratio. When the viscosity relative increment is related to the concentration by mass of the substance dissolved in the solution, pi, the concentration-related viscosity relative increment, J, called Staudinger function (viscosity number), is obtained. 1 lV=(%-l)- ( 2) pi The concent
7、ration by mass, Pi, is mostly expressed in g/cm3, the Staudinger function, J, in cm3/g. 3 Calculation of viscosity relative increment and Staudinger function From flow times measured by the Ubbelohde viscometer, the kinematic viscosity, u, which is the ratio of dynamic viscosity, q, to density, e, i
8、s immediately obtained. Provided that the differences in density between the solvent and the solution are small, J, can be calculated from the ratio of the kinematic viscosities or that of flow times which are proportional to these viscosities. (3) IV= - .- (i I) ;i where t t, Only flow times correc
9、ted in accordance with clause 5 shall be used for 1 and t, in equation (31, not the flow times measured. is the flow time of the solution; is the flow time of the solvent. Continued on pages 2 to 5 Beuih Varlag GmbH. Berlin. has the exclusive right of sala for German Standards (DIN-Normen). DIN 51 5
10、62 Part 3 Engl. Price group 6 05.87 Sales No. O106 Page 2 DIN 51 562 Part 3 4 Hagenbach correction If the actual flow time is shorter than the minimum flow time to1 specified in DIN 51 562 Part 1, the individual values for the Hagenbach correction, A tHi, are to be determined for every capillary vis
11、cometer using suitable standard liquids of known viscosity, as follows: where tni is the flow time measured using the standard liquid, i; vi is the kinematic viscosity of the standard liquid; K is the apparatus constant of the viscometer. In accordance with DIN 51 562 Part 1, the flow times and the
12、Hagenbach corrections shall be expressed in s, the kinematic viscosities in mm2/s “1 and the apparatus constants in mm2/s2. By linear interpolation between thevalues ofAtH1 andAtHz determined for the two standard liquids i = 1 and i = 2 having flow times te, and tez respectively, the Hagenbach corre
13、ction A t, shall be calculated for another flow time, te, using equations (5) and (6) (see also figure 1): (5) (6) tg2 tg1 Flow time tg shall lie between flow times fel and tap. Curve a -correction equation (3) as in DIN 51 652 Curve b -true form of the individual Hagenbach Curve c - straight line t
14、o be interpolated from Part 1 (validity ranged) correction equation (5); it intersects curve b at points Figure 1. Example of the individual Hagenbach correc- tion for an Ubbelohde viscometer No. Oc in accordance with DIN 51 562 Part 1 Figure 1 represents an example of a typical form of the individu
15、al Hagenbach correction for an Ubbelohde viscometer No. Oc in accordance with DIN 51 562 Part 1, in which the transition from the capillary to the suspended level is funnel-shaped. 5 Correction of the measured flow times To determine the Staudinger function (viscosity number) by equation (31, the me
16、asured flow times of the solvent, te, and the solution, te, shall be corrected using the Hagenbach correction in accordance with clause 4 (see equations 7 and 8). ts = tgs - A tHs, t tg -AtH and (7) ( 8) where the subscript s represents the solvent. 6 Limitation of correction method For Ubbelohde vi
17、scometer No. O in accordance with DIN 51 562 Part 1, the method is applicable for the shortest flow times attainable in practice. For all other viscometers, attention shall be paid in cases of short flow times (see table 1) to disturbances which announce the imminent collapse of the suspended level.
18、 Figure 2 illustrates these disturbances in a simplified form. Table 1. Limiting values of the measured flow time, tg, and the Reynolds number, Re, in accordance with DIN 53 012, up to which generally no suspended level disturbances occur Ubbelohde viscometer as in DIN 51 562 Part 2 Limiting value o
19、f t, in s Corresponding Reynolds number Re Note. In some viscometers, the disturbances can occur even at slightly longer flow times, although the visual examination of the lower end of the capillary does not suggest such disturbances. 7 Apparatus and reagents The following apparatus and reagents sha
20、ll be used. 7.1 Ubbelohde viscometer with suspended level in accordance with DIN 51 562 Part 1. For measuring polymer solutions, viscometers shall be used for which the surface tension correction is sufficiently small (see also Explanatory notes). Viscometers with a lower capillary end, which is eit
21、her sharp-edged or funnel- shaped, may also be used. To reduce uncertainty of measurement, automatic measuring devices for the determination of flow times shall preferably be used. Determination of the Hagenbach correction shall be carried out in the same order as the tests. 7.2 Thermometer in accor
22、dance with DIN 51 562 Part 1. *) Previously centistokes (cSt); 1 cSt = 1 mm2/s. DIN 51 562 Part 3 Page 3 d) a) Undisturbed flow, measurement is usable b) Commencement of a disturbance at an excessively high flow rate c) Progress of the disturbance at an even higher flow rate d) Collapse of the suspe
23、nded level Figure 2. Formation of the suspended level The illustration shows the liquid alone without the glass wall of the viscometer enclosing it. Measurement cannot be used 7.3 Constant-temperature liquid circulator as specified in DIN 12 879 Part 1, capable of maintaining the test temperature co
24、nstant to within 0,Ol OC. See DIN 51 562 Part 1 for further details. 7.4 Timing device with an uncertainty of measurement of 0,02 s. The time base of the electronic measuring device shall be constant to to the nominal value. and shall correspond 7.5 Two to three lowviscosity standard liquids (see Ex
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