Dual-Axis Centrifugal Mixer - A Better Mix

Jacketed tanks/reactors are commonplace in the chemical industry. Many batch operations in the chemical industry require both heating and cooling at different times in the process. Rapid changes in temperature of the heat transfer media can thermally shock the equipment. Typically, thermal shock is defined as changing the cooling or heating media at the jacket inlet more than 25 F per minute. Thermal shock can be avoided by tempering the heat transfer media and providing proper venting. Tempering is easiest achieved when a common heat transfer media is used for both heating and cooling. A Temperature Control Unit (TCU) can be used to adjust the temperature of the heat transfer media at a rate that does not pose the risk of thermal shock. While TCUs are the simplest means of controlling temperature and protecting equipment many companies still insist on using different media for heating and cooling. Many times this includes steam heat and water cooling. If this MUST be done some minimum precautions should be taken.

1. HEATING to COOLING:

When changing from steam heating to cooling water one of the following procedures should be followed:

A. Forced Tempering

Vent steam out of jacket and drain condensate. Allow jacket cool down naturally or use compressed air to blow-down the jacket from top to bottom to achieve correct temperatures. Close vents and slowly introduce hot water at the correct temperature to the jacket. Increase flow rate to process conditions and decrease water temperature at a rate of less than 25 F per minute.

B. Natural Tempering

Vent steam out of jackets and completely drain all condensate. Allow the jacket to cool down naturally to the correct temperature. Close vents and introduce cooling water.

2. COOLING to HEATING:

When changing from cooling water to steam heating one of the following procedures should be followed:

A. Forced Tempering

Raise circulating water temperature in the jacket at a rate of less than 25 F per minute until desired steam temperature is reached. Vent jackets and completely drain out water. Close vents and slowly introduce steam into the jacket.

B. Natural Tempering

Vent and drain water out of jackets. Let the jacket warm up naturally to the correct temperature. Slowly introduce steam into jackets at reduced pressure and/or flow rate (temperature) until the desired steam temperature is reached. As with any manual process, there are risks associated with this.

Review of the function and operation of planetary-centrifugal mixers. Published July 2010, Adhesives and Sealants Industry Magazine

The axial flow paradigm has long been one of the most predominant mechanisms of mixing. This flow pattern is generally produced by a single-shaft mixer with axial flow impellers. It is characterized by flow down the center of the batch to the bottom of the tank, which is then deflected outward toward the wall by the container bottom. It then travels up the vessel wall and back across the surface, as shown in Figure 1.

Fig. 1: Axial Flow in a Single Shaft Mixer

The single-shaft mixer has limited use in the preparation of adhesives and sealants, as the axial flow patterns are difficult to reproduce in the high viscosities these products typically exhibit. When viscosity rises, mixing efficiency drops as the distance from the mixing blade increases. Increasing the blade speed does little to compensate for the loss of flow at the outer reaches of the tank. In addition, vortexes become deeper as speed increases, resulting in air entrainment. To overcome these limitations, multiple shafts were introduced to provide both the shear and flow necessary to produce a uniform product. Multiple-shaft mixers are common in the production of adhesives and sealants. However, these multi-shaft mixers do not produce the same flow patterns. They also require additional clean-up, limit the ability to produce small batches, and do not always mix as efficiently in small sizes as larger production machines. In many cases, the only option available has been to manually assist the mixer or manually mix all together.

DUAL-AXIS CENTRIFUGAL MIXERS

The dual-axis centrifugal mixer uses no shafts. Instead, it relies on two distinct rotational vectors and angular alignment of the mixing container to produce its mixing ability (see Figure 2). First, a mixing container is held at a fixed distance from a center axis; the container orbits that axis at high speed. (If this were the only axis of rotation, the unit would effectively operate as a centrifuge, separating products based on density.) To complement this motion, the container rotates about its own center axis and the cup is angled toward the motor axis. This second axis of rotation and cup angle is essential to the generation of the mixing action. Figure 2: Interior of a Dual-Axis Centrifugal Mixer

The surface of the water in a cup remains perpendicular to the force of gravity, acting on it regardless of the angle at which the cup might be held. The surface of the material in the mixing container will remain perpendicular not to the force of gravity, but to the stronger centrifugal force created by the orbital speed of the container. The centrifugal force is a function of the distance from the center of rotation and the angular velocity. The dual-axis centrifugal mixer develops centrifugal acceleration in the range of 400 G. Due to the angle at which the cup is held, the distance between the center machine axis and any point on the surface of the product continually changes as the cup rotates. Product flows to compensate for these changes, resulting in flow patterns from the edge of the container to the center of the batch.

SURFACE FLOW

The mixing action of the dual-axis centrifugal mixer can be demonstrated with white and blue samples of children’s modeling compound. Approximately 80 grams of the blue and another 80 of the white were rolled into a ball, flattened into “hockey pucks” and placed into the mixing cup, with blue on the bottom and white on the top. The flow pattern observed in a traditional single-shaft mixer includes a vortex in or around the center of the mixing container.

[caption id="attachment_637" align="aligncenter" width="300"] Figure 3: Surface Flow Pattern[/caption]

As shown in Figure 3, this same flow pattern can be seen in the dual-axis centrifugal mixer. A center vortex forms and material travels down that vortex. The vortex, while present, remains shallow as the flow is created by centrifugal force acting on the product as a whole, instead of induced by a relatively small blade operating within the batch. The vortex is most evident in the T015 (time = 15 seconds) photo. Prior to the final photo, T135 (2 minutes, 15 seconds), surface eddies begin to form to further improve mixing as viscosity is reduced. Similar flow patterns can be seen in traditional liquid mixing when the mixing shaft is offset.

INTERNAL FLOW

Similarities are also evident within the batch, as can be seen when the mixed sample is cut in half (see Figure 4). The material travels down the center of the product and is deflected outward toward the wall by the container bottom. It then travels up the vessel wall and back across the surface of the product, as described in the previous section. [caption id="attachment_638" align="aligncenter" width="300"] Figure 4: Internal Flow Pattern[/caption] After T015 (15 seconds), the blue material, which was originally at the bottom of the container, has traveled up the wall of the vessel, across the top, and down the center of the product. By T030 (30 seconds), a mixture of blue and white material follows a similar path. This mixing continues until T135 (2 minutes, 15 seconds) when a uniform product is produced.

REAL-WORLD MIXING

This type of mixer functions well in real-world operations, which often requires the mixing of many dissimilar components. Figure 5 illustrates the mixing of a series of powders, pastes, and liquids at a total mix time of 45 seconds. Typically, a 20-minute batch time is considered excellent for a traditional shaft-type mixer with much lower viscosities. [caption id="attachment_639" align="aligncenter" width="300"] Figure 5: Powder, Paste and Liquid Mixing[/caption] The dual-axis centrifugal mixer produces the axial flow patterns that are predominant in liquid mixing while overcoming the viscosity limitations of a traditional single-shaft mixer. Added benefits include reduced cleanup requirements, as all shafts are eliminated and the container remains the only contact part. Without shafts, it is possible to produce very small batches; standard units are capable of mixing batches as small as 50 grams and as large as 2,500 grams. (These batch limits can be extended with container adapters.) In addition, the shallow vortex eliminates additional air entrainment during mixing. As vortex depth is not a limiting factor, the dual-axis centrifugal mixer can mix at high energy levels, which results in shorter batch times. In the adhesive and sealant industry, the mixer has been used for fast and efficient formulation qualification, pilot development, and small batch production.

Schmidt, Stephen T. "A Better Mix" Adhesive andamp; Sealants Industry Magazine, 1 July 2010.