

Torque Rheometer for Polymer Compounding
聚合物混炼用转矩流变仪
- SKU RHE-0004
- Rheometers
- CE (to be confirmed)
- ISO 9001 manufacturing (to be confirmed)
Price on request — FOB / CIF quoted per order
Prices depend on configuration, quantity and destination port.
Key specifications
| Chamber volume | 30–300 mL (typical 60 mL) |
|---|---|
| Rotor speed | 0–200 rpm |
| Torque range | 0–200 N·m |
| Torque resolution | 0.01 N·m |
| Temperature range | Ambient to 400 °C |
| Temperature accuracy | ±1 °C |
By Lab Manufacturers China Technical TeamLast reviewed Standards: ISO 3219, ISO 11443, ISO 6721-10
What is the Torque Rheometer for Polymer Compounding?
A torque rheometer mixes polymer compounds in a heated chamber with rotating rotors and records the torque needed to keep them turning. It tracks fusion, gelation, crosslinking and degradation, and is used for PVC dry-blend and compounding formulation work.
What is the Torque Rheometer for Polymer Compounding?
A torque rheometer mixes polymer compounds in a heated chamber with rotating rotors and records the torque needed to keep them turning. It tracks fusion, gelation, crosslinking and degradation, and is used for PVC dry-blend and compounding formulation work.
Overview
The instrument consists of a heated mixing chamber, one or two rotors of defined geometry, a torque transducer on the drive and a temperature control system. Polymer powder or granulate is loaded, compacted by a ram and mixed while torque and melt temperature are logged. A PVC fusion curve shows a torque peak as the grains break down, then a steady value reflecting melt viscosity, and any rise later in the run indicates crosslinking or degradation. Because the sample form is powder, granules or flakes, the test needs no compression moulding, and a single run uses 30 to 300 g depending on chamber size. The same drive can carry a single-screw extruder or a capillary die attachment, so ribbon, film or rod can be produced from the same sample for further testing.
How does it work?
A rheometer applies a controlled deformation to a polymer sample and measures the resulting force or torque. Rotational instruments use parallel plates, cones or concentric cylinders and can work in steady shear, giving shear viscosity against shear rate, or in oscillation, giving storage and loss moduli against frequency. Capillary instruments force melt through a die of known diameter and length at a controlled piston speed, measuring pressure to calculate apparent shear viscosity at shear rates that reach those of real extrusion. Torque rheometers mix material in a heated chamber and record the torque needed to turn the rotors, which tracks gelation, fusion and degradation in a compounding context. The choice depends on the shear rate range, the sample form and whether elasticity or only viscosity is required.
What are the key features?
- Heated mixing chamber with one or two rotors
- Torque and melt temperature recorded against time
- Chamber volumes from 30 to 300 mL
- Interchangeable extruder and capillary die attachments
- Detection of fusion, crosslinking and degradation
- Accepts powder, granulate and flake samples directly
What are the technical specifications?
A typical torque rheometer for polymer compounding configuration offers chamber volume of 30–300 mL (typical 60 mL), rotor speed of 0–200 rpm, torque range of 0–200 N·m, torque resolution of 0.01 N·m, temperature range of Ambient to 400 °C and temperature accuracy of ±1 °C. Values are indicative of the product class; the exact figures for each configuration are confirmed on the quotation and the calibration documents supplied with the instrument.
Which applications is it used for?
The Torque Rheometer for Polymer Compounding is used in PVC dry-blend fusion and stability testing, compounding formulation development, masterbatch dispersion studies and thermal stability under shear of filled compounds. Across the wider Rheometers class, laboratories also deploy it for molecular weight and molecular weight distribution comparison, processing behaviour prediction for extrusion and moulding and filler and additive effect on melt viscosity.
Which standards and certifications apply?
Relevant standards and methods include ISO 3219, ISO 11443, ISO 6721-10, ASTM D3835, ASTM D4440, ASTM D2538 and IEC 61010-1. Certification candidates for this model are CE and ISO 9001 manufacturing; each is to be confirmed for the specific configuration before shipment, and certificates are supplied only where they have been issued.
Sample preparation dominates repeatability: dry hygroscopic polymers, compression-mould discs of defined thickness for rotational testing, and ensure filled samples are homogeneous. Set the gap and check it with a zero-gap routine before each series, because a small gap error changes the calculated viscosity. In capillary work, verify piston speed and pressure transducer calibration, and apply the Bagley and Rabinowitsch corrections when true viscosity is required. Purge the oven with nitrogen for high-temperature or oxidation-sensitive polymers. Clean dies and plates thoroughly, since degraded residue changes the surface and the measured torque, and record temperature, geometry and gap with every result.
How do I select the right Torque Rheometer for Polymer Compounding?
Choose a torque rheometer when the question is about compounding behaviour rather than a fundamental viscosity value, or when only powder or granulate samples are available. Match chamber volume to the sample mass you can produce; a 60 mL chamber is usual for development work, while larger chambers suit production-scale formulations. Ask whether extruder and capillary die attachments are available, since they let one instrument cover mixing and flow testing.
How does it compare with other Rheometers variants?
Match the instrument to the shear rate range that governs your process. Rotational rheometers cover low shear rates and are the only option when viscoelastic data, yield stress or normal force are required, making them suitable for molecular weight comparisons and additive studies. Capillary rheometers reach the high shear rates of extrusion and injection moulding and are more tolerant of filled and highly viscous materials. Torque rheometers are used when the question concerns compounding behaviour, gelation or thermal stability under shear rather than a fundamental viscosity value. Inline instruments are selected for continuous process monitoring and never replace laboratory characterisation, because they see only one fixed measurement point.
Full specifications
| Chamber volume | 30–300 mL (typical 60 mL) |
|---|---|
| Rotor speed | 0–200 rpm |
| Torque range | 0–200 N·m |
| Torque resolution | 0.01 N·m |
| Temperature range | Ambient to 400 °C |
| Temperature accuracy | ±1 °C |
| Typical sample mass | 30–300 g depending on chamber |
| Melt temperature sensor | Embedded thermocouple in chamber |
| Data output | Torque, temperature and energy curves |
| Power | 3–7 kW |
Indicative values for this product class. Final specifications are confirmed on the quotation and in the calibration documents supplied with the instrument.
Applications
- PVC dry-blend fusion and stability testing
- Compounding formulation development
- Masterbatch dispersion studies
- Thermal stability under shear of filled compounds
Key features
- Heated mixing chamber with one or two rotors
- Torque and melt temperature recorded against time
- Chamber volumes from 30 to 300 mL
- Interchangeable extruder and capillary die attachments
- Detection of fusion, crosslinking and degradation
- Accepts powder, granulate and flake samples directly
Frequently asked questions about Torque Rheometer for Polymer Compounding
Torque rises as the rotors begin to work the dry blend, peaks when the primary particles break down and the mixture fuses, then settles to a plateau reflecting melt viscosity. A long time to peak indicates poor gelling, while a rising plateau indicates crosslinking or degradation, so both the time and torque values are reported.
Larger chambers hold more material and generate more torque, and the shear rate distribution differs from a smaller chamber, so curves are only comparable when recorded in the same chamber at the same rotor speed and fill factor. Fill factor, defined as the volume fraction of material loaded, should be reported with every curve.
Yes, mixing is one of the main uses. After the recorded run the compound can be removed and compression moulded into plates or, with an extruder attachment, drawn as ribbon or rod. This allows one instrument to prepare and characterise a formulation, which is efficient when material is scarce.
A rotational rheometer measures viscosity in steady or oscillatory shear at low shear rates, where the material response is dominated by molecular relaxation. A capillary rheometer measures at high shear rates that match extrusion and injection moulding. The two techniques overlap in a mid-range and should agree after corrections, but each covers a shear rate window the other cannot reach.
Viscosity is calculated from measured torque, angular velocity and the gap between the geometries, so an error in gap propagates directly into the result. Compression of the sample and thermal expansion change the effective gap, which is why a zero-gap routine and a constant sample thickness are used before each series.
They can, but filler particles may slip at the plate surface, settle, or bridge the gap, so the measured viscosity can be too low. Practical measures are to use serrated or roughened plates, larger gaps, and lower filler loadings where possible, and to compare results only between samples of the same filler content and particle size.
Related models






