The present invention relates to rheometers and more particularly to couette rheometers for testing rheological properties of a fluid sample (liquid, slurry, gel or powder mix, hereafter “fluid”) in a sample cup.
Several forms of couette rheometer are extant in the prior art including the Brookfield Engineering Laboratories (assignee of the present invention) models PVS and Thermosel. In all of these, a spindle is contained within a cup filled partially with the fluid sample material, typically a liquid and a relative rotation is established between the cup and spindle, driving one while the other is a fixed sensing element and heating the sample by conduction from a heat source to and through the cup. In one form, the cup is rotated and the spindle is at the end of a sensing shaft and fixed to ground via a torque transducer for limited angular deflection that can occur through the sample fluid. In another form, the spindle is driven and the cup is fixed.
Generally, the prior art is unable to provide a stable heating of the sample material to enable rheology measurements at a stably maintained elevated target temperature, e.g., 260° C., or higher. There is therefore a need to overcome this limitation.
A rheometer instrument with a rheometer unit insertable into and removable from a heating unit is provided along with the latter unit, constructed to provide a heating of the sample cup portion of the rheometer unit by radiant heating—as a replacement for traditional heated liquid bath of water or alcohol (e.g. glycol) solution) from the inner surface diameter of a cup well receiving well (chamber) within a heating block of the heating unit. The chamber has an inner surface that substantially surrounds and is in closely opposing relation to the outer diameter surface of the sample cup of the rheometer unit). The two opposing surfaces are coated or otherwise constructed or modified to produce emissive/absorption surfaces, typically with the inner diameter surface of the heating unit chamber having a smooth, machined surface spray painted with fiat black high temperature silicone based paint and a sample cup outer diameter being sand blasted with 100-180 grit and coated with a flat/matte ceramic coating. Reference to inner and/or outer “diameter surfaces” herein can include flat or other non-circular shapes as well as circular shapes, e.g. where the sample cup and surrounding chambers are rectangular in cross section.
These methods are controlled to produce a range of emissivity, absorption coefficients at each of the opposing surfaces of the radiant heating process in a preferred range of 0.8 to 0.97.
Tests have shown this radiant heating approach to be just as effective as prior art liquid external baths without difficulties of such external baths and to reduce duration of achieving target high temperatures and to increase reliability of attaining and maintaining highest target temperatures.
Other features and advantages of the present invention will be apparent from the following detailed description of various embodiments taken in conjunction with the accompanying drawings in which:
One embodiment of the rheometer instrument of the present invention shown in
The base assembly contains power supply and signal processing elements of the instrument. Conduits 207 for coolant water or other fluid are provided in the heating unit 200 with ports at 206 and the fluid is supplied through the ports to the heating unit by a user. A vertical slide assembly 310 is provided. It has an axially slidable part 312 and fixed part 314 mounted on a stand which can be seated on the base unit or on a lab table or floor and is constructed to provide stable support. Other terms of holding slide assembly can be provided. The slidable part carries the rheometer unit out of the heating unit up out of the rheometer or lower the rheometer unit down into it as shown in
The rheometer unit per se is substantially similar to the Brookfield Engineering Laboratories Inc, long extant (in the U.S. and abroad) model PVS rheometer.
The heating unit 200 comprises a brass heat chamber 210 surrounded by an insulator cylinder 212 and seated on an insulating block 214 is a heating block 216 with a temperature sensor 216A and an overtemperature switch 216B (e.g. a bi-metallic element) is mounted to the base. A cooling block 218 with internal conduits for coolant liquid enables quickly cooling the heating unit between tests.
A ceramic insulator 222 is provided. A felted thermoset fibrous resin (e.g. DuPont's Kevlar® brand aramid fiber) 224 is provided to keep the heated air between the bath chamber and sample cup from escaping too quickly.
Instead of having a surrounding liquid bath as in conventional practice to heat the cup entirely by conduction from the bath, the present invention uses radiation as a replacement. The structure for effecting radiant heating includes a heater band 220 (preferably made of mica), an emissive coating on the interior diameter 210D of the heat block's central well. In turn the outer diameter 104D of the sample cup has an absorptive coating.
The emissive coating silicone based high temperature flat Hack paint.
The absorptive coating is the well known polymer matrix high temperature ceramic coating system exemplified by Cerakote™ brand coating of NIC Industrial Co., White River, Oreg. and applied as a matte/black ceramic coating.
The heater band rated at 500 watts is made of mica.
Testing of the radiant heating unit shows the necessity for the heat emitting/absorbing coatings on the sample cup exterior surface and heating block cup well inner surface. This emissivity coefficients of both should be in the 0.8-0.97 range.
Tests were conducted at 5, 10 and 250 rpm of cup rotation for such surfaces as (a) unpainted and (b) both painted with black emissive/absorptive coatings as described above in an effort to achieve cup/sample temperature of 260° C. in a reasonable time through use of the mica heater and heating block with the heater powered at 500 watts. The results were as shown in Table 1 below:
1(i) aborted at 235° C. after 110 minutes and (ii) aborted at 238° C. after 96 minutes and (ii) aborted at 238° C. after 90 minutes
In the above testing and in a commercial scale embodiment the temperature of the heating block was and is accurate from room temperature up to 340° C. to maintain an adequate heat flux to reliably maintain selected sample temperatures.
Sensing of temperature should be done in commercial units both at the sample fluid and in the bath heat chamber of the heating unit.
As noted above the instrument heater is at a higher temperature vs. target sample temperature, e.g. 340° C. heater temperature vs, a 260° C. target sample heat temperature. Measurements of sample and heating block temperature are used in the PID control or sample temperature near the target temperature (e.g. 260° C.) to attain a product reach to the target temperature and minimize over-shoot and upon reaching target temperatures to maintain minimum if any deviation by raising, lowering the level of supplied heating. Between tests quick cooling can be expedited by the coolant fluids passed in and out of the rheometer unit via ports 206 and conduits 207.
It is thus seen that a radiant heating approach is feasible and can achieve all that is achieved in prior art baths without the difficulties of an external liquid bath for heating (weight, volume, orientation sensitivity, etc.)
It will now be apparent to those skilled in the art that other embodiments, improvements, details, and uses can be made consistent with the letter and spirit of the foregoing disclosure and within the scope of this patent, which is limited only by the following claims, construed in accordance with the patent law, including the doctrine of equivalents.
This application claims the benefit of priority to U.S. Provisional Application No. 61/792,612, filed on Mar. 15, 2013, the entire contents of which are incorporated herein by reference for all purposes.
Number | Date | Country | |
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61792612 | Mar 2013 | US |