Speciality silica powders as liquid carriers – converting liquids into dry flowable powders

Blog Archive | 10 minutes  | Author: Adam Morgan , Ph.D.

What are silica carriers? In what systems can I use them?

A versatile range of precipitated (SIPERNAT®) and fumed (AEROSIL®) silicas are available from EVONIK for absorbing liquids, such that they are converted into dry free-flowing powders. Why are these products highly efficient carriers for liquids? It is due to their high internal and interstitial pore volume. Many other materials commonly used as carriers only have external surface area available, for example, maltodextrin and starches (Figure 1).

Porous silica carrier vs. non-porous carrier material

Figure 1. Schematic of liquid at the surface of a non-porous carrier (left) and of liquid absorbed in the pores of SIPERNAT® (right).

 

Grades can be chosen with different particle sizes, depending on the requirements of the end application. SIPERNAT® 22 and 2200 are very coarse grades, which are more free-flowing and less dusty than some other products. They may be too large for certain applications, however. In this case, the formulator might choose SIPERNAT® 22S, SIPERNAT® 50S or AEROSIL® 200. Conversely, these grades may be too fragile or dusty for particular applications.

Lawrence Industries technical sales team will be able to assist you with selecting the correct grade for your application. Please call us on 01827 314151.

Table 1 gives an overview of relevant physicochemical characteristics displayed by some of these carriers.

physicochemical properties of silica carriers from Evonik

Table 1. Typical physicochemical data of some selected silica carrier grades.

 

It is possible to convert liquid, semi-solid and pasty substances into powder. Table 2 gives an overview of some frequently converted absorbates and recommends the typical addition level ranges for some commonly used grades in these applications.

Typical liquids that can be absorbed by silica carriers

Table 2. Application areas of speciality silica as a carrier.

 

How to dose liquid onto the silica carriers

Generally, the carrier should be put into the mixer first. Liquids should be dosed in as continuously and finely distributed as possible. In some special cases, where the absorbate has been liquefied through increased temperature, improved results can be obtained wherein the silica is added to the liquid.

It is important that gentle mixing is applied. Optimum results cannot usually be obtained with high pressure or high shear forces as they partly destroy the porous structure, desorbing any absorbed liquid.

Figure 2 shows a choline chloride formula with 67% choline chloride solution (75%) absorbed on 33% SIPERNAT® 22 by weight. This was produced at low shear and resulted in good flow behaviour, enabling the material to be easily packed, transported and processed further.

free flowing choline chloride absorbed onto a silica carrier

Figure 2. Free-flowing choline chloride absorbate onto SIPERNAT® 22 as a carrier.

In comparison, the same choline chloride system was processed under high shear. The results of this can be seen in Figure 3. This is not an ideal system for flow behaviour.

Pasty choline chloride absorbed onto silica due to overshearing

Figure 3. Choline chloride paste created by excessive shear when loading the liquid onto SIPERNAT® 22.

To optimise flow behaviour and pressure stability of the absorbates, the liquid should be introduced as finely divided as possible. The best method is to atomise the liquid through a sprayer. If this is not possible then dripping is better than pouring. Ploughshare® and paddle mixers are well suited to perform these kinds of mixing tasks. They have short mixing times and very low shear, so the particles remain intact. Avoid high-intensity mixing elements inside low shear equipment.

For fine particle carrier silica, the absorption capacity may vary a lot depending on the shear energy which is applied when the absorbate is made. Overshearing these products can lead to a reduction in the absorption capacity; due to damage done to the particle structure and uncontrolled agglomeration. Figure 4 illustrates the absorption capacity for some selected silica carriers. This is given as the maximum volume of liquid (ml/g of silica) before liquid soaks out under pressure.

absorption capacities of common silica carriers

Figure 4. Maximum absorption of selected SIPERNAT® types. For fine particle silica, the absorption capacity depends on the mixing conditions.

 

Some noteworthy observations when making absorbates:

  • A low energy mixing device that fluidizes the dry carrier powder with minimum shear often works best but this depends on the physical properties of the liquid. Suitable mixers include ribbon, ploughshare® or V-type “liquid-solid” blenders. Conical or Nauta®-type mixers are also suitable.
  • In some cases, high shear can be used with caution – if the liquid has a high melting point and will solidify into agglomerates, with silica particles surrounding the droplets.
  • Generally, larger particle size grades have better flow properties. For some applications, such as in instant beverages, small particles are desirable; as they allow the powder ingredients to dissolve in the mixture without affecting flavour or texture.
  • Consider protecting the liquid from oxidation. High surface area materials can accelerate oxidation in unsaturated ingredients. In this case, choose a lower surface area SIPERNAT® or AEROSIL® product - or add an anti-oxidant to inhibit oxidation.

 

Optimize flowability and dustiness with the right loading level

As loading level increases, flowability reaches an optimum. This will depend on the properties of the carrier silica and the liquid being carried. When saturated, the carrier flow will become worse and dustiness is reduced. This effect is shown through two case studies, in Figure 5 and Figure 6. It is important to choose the carrier based on the required liquid loading level since each carrier will exhibit an optimum loading level where efficiency, flow and dustiness are balanced.

dustiness of silica carriers vs. loading of absorbate

Figure 5. SIPERNAT® 50 absorbate of a nutraceutical active ingredient. Dustiness is defined as the percentage light scattering at 30 seconds when the sample is dropped in the sample chamber of a Palas Dustview™.

SIPERNAT absorbing Vitamin E

Figure 6. SIPERNAT® 22 absorbing Vitamin E, versus competitive silica.

 

When mixing both SIPERNAT® and other substances, dual-carrier applications are possible. These types of carriers can optimise cost, absorption capacity, dustiness and various other desired properties. For example, a dual-carrier made of maltodextrin and SIPERNAT® 500 LS can optimize absorption capacity, costs, solubility and flavour profiles. The specific combination of dual carriers is dependent on several factors and needs to be based on the desired finished product. These factors include:

  • Absorption capacity of each carrier material.
  • Density of each carrier material.
  • Density of the liquid to be plated.
  • Volatility of the liquid.
  • Amount of insoluble material that can be tolerated in the system.

 

Flavour Applications

Flavour control is critical in the beverage and food industries since evaporative losses will impact the final product. This may occur either during manufacture or storage.

Kinetic considerations are significant when choosing a substrate to carry liquid flavours. Encapsulation techniques can be used to control these losses.

A study was conducted to investigate the effect of carrier type on the evaporation rate of a volatile flavour compound. Five SIPERNAT® grades and one AEROSIL® grade were compared to a competitive silica and silica gel. Thermogravimetric analysis (TGA) was then used to measure the loss of volatiles over time (Figure 7).

evaporation rates of volatile flavours from different silica carriers

Figure 7. Evaporation rate of a flavour with various silica treatments at 25°C.

 

All of the SIPERNAT® and AEROSIL® substrates released the flavour at rates slower than the evaporation of the original flavour compound. Evaporation rate was found to be approximately proportional to the surface area of the carrier silica used. Silica gel was the worst-performing substrate. These products can be combined with various encapsulation techniques to improve performance further.

 

Summary and what to do now

SIPERNAT® and AEROSIL® silicas have a high pore capacity, which enables them to efficiently convert liquids into free-flowing powders. There are many considerations as to which grade should be chosen and this article aims to suggest some good starting points and questions to consider for your application. However, no article can replace the knowledge of our technical sales team - so call us today on 01827 314151, to see how we can help you with your next formulation challenge.

This article has been adapted from two pieces of EVONIK literature: TI 1367 and TI 1213.

Author: Adam Morgan , Ph.D.

Adam studied chemistry at the University of Warwick for 8 years, where he obtained a Ph.D. in the field of polymer and inorganic colloid science. He has been with Lawrence Industries since 2014 as a technical sales manager covering all industry areas. He is now responsible for marketing within the company as well.