Skip to Main Content
Skip Nav Destination
ASTM Selected Technical Papers
Symposium on Non-Newtonian Viscometry
By
ASTM Committee D-2
ASTM Committee D-2
Search for other works by this author on:
ISBN-10:
0-8031-6116-6
ISBN:
978-0-8031-6116-0
No. of Pages:
163
Publisher:
ASTM International
Publication date:
1962

The design and construction of a versatile capillary high-shear viscometer is described. Use of nitrogen pressure as the driving force and of a single pass through the capillary completely eliminate all areas of nonstreamline flow from the viscometer. By using interchangeable capillaries and efflux bulbs, the viscometer has a temperature range of -65 to 300 F, a viscosity range of S to 1 million centipoises, and a rate-of-shear range of 1 to 1 million reciprocal seconds. The maximum shearing stress for the three capillaries described varies from 92,000 to 300,000 dynes per sq cm.

Calibration techniques with Newtonian hydrocarbon fluids are described. Temperature and pressure effects of both Newtonian hydrocarbons and non-Newtonian polymer solutions are evaluated in capillary instruments.

Non-Newtonian data for the PRL (Petroleum Refining Laboratory) single-pass viscometer, using ASTM oils 103 and 104, are compared with similar data for the Kingsbury tapered plug viscometer and for the PRL high-shear viscometer.

High-shear-rate viscosity measurement of polymer solutions without permanent viscosity change is demonstrated. The effects of polymer type, polymer molecular weight, and solvent type are illustrated, using the PRL single-pass viscometer.

1.
Richards
R. B.
, Ph.D. Thesis,
The Pennsylvania State University
(
1946
).
2.
Foehr
E. J.
, M.S. Thesis,
The Pennsylvania State University
(
1941
).
3.
Chadwick
G. F.
, M. S. Thesis,
The Pennsylvania State University
(
1954
).
4.
Fenske
M. R.
,
Klaus
E. E.
, and
Dannenbrink
R. W.
, “
The Comparison of Viscosity-Shear Data Obtained with the Kingsbury Tapered Plug Viscometer and the PRL High Shear Capillary Viscometer
,” Symposium on Methods of Measuring Viscosity at High Rates of Shear, ASTM STP No. 111,
Am. Soc. Testing Mats.
, p. 45 (
1951
).
5.
Jolie
R. M.
, Ph.D. Thesis,
The Pennsylvania State University
(
1957
).
6.
Fenske
M. R.
,
Klaus
E. E.
, and
Dannenbrink
R. W.
, “
Viscosity-Shear Behavior of Two Non-Newtonian Polymer-Blended Oils
,” Symposium on Methods of Measuring Viscosity at High Rates of Shear, ASTM STP No. 111,
Am. Soc. Testing Mats.
, p. 3 (
1951
).
7.
Klaus
E E.
and
Fenske
M. R.
,
Lubrication Engineering
 0024-7154, Vol.
11
, p. 101 (
1955
).
8.
Klaus
E. E.
,
Jolie
R. M.
, and
Fenske
M. R.
, Am. Soc. Mechanical Engrs. Annual Meeting, paper No. 58-1-294,
New York, N.Y.
, Dec., 1958.
9.
Am. Soc. Mechanical Engrs. Pressure Viscosity Report, Vols
1
and
2
, New York, N.Y. (
1953
).
10.
Hersey
M. D.
and
Hopkins
R. F.
, “
Viscosity of Lubricants Under Pressure
,”
Am. Soc. Mechanical Engrs.
(
1954
x).
11.
Petroleum Refining Laboratory, The Pennsylvania State University
, unpublished data.
This content is only available via PDF.
You do not currently have access to this chapter.
Close Modal

or Create an Account

Close Modal
Close Modal