Method for the production of commercial nanoparticle and micro particle powders

a nanoparticle and powder technology, applied in the direction of biocide, grain treatment, drug composition, etc., can solve the problems of poor bioavailability, high dissolution rate, poor soluble active agent safety, etc., and achieve the effect of reducing static charge, reducing cohesiveness profile, and superior product flow characteristi

Inactive Publication Date: 2012-06-28
ICEUTICA PTY LTD
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  • Abstract
  • Description
  • Claims
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AI Technical Summary

Benefits of technology

[0026]Preferably, the powder handling characteristics of the biologically active material produced by this invention are superior to the powder handling characteristics of a biologically active material with the same, similar or larger particle size manufactured using a conventional process. Preferably, the biologically active material subject to this invention has superior product flow characteristic compared to the product flow characteristic of a biologically active material with the same, similar or larger particle size manufactured using a conventional process. Preferably, the biologically active material subject to this invention has a lower static charge compared to the static charge of a biologically active material with the same, similar or larger particle size manufactured using a conventional process. Preferably, the biologically active material subject to this invention has a lower cohesiveness profile compared to the cohesiveness profile of a biologically active material with the same, similar or larger particle size manufactured using a conventional process. Preferably, the biologically active material subject to this invention has a lower propensity for aggregation compared to the propensity for aggregation of a biologically active material with the same, similar or larger particle size manufactured using a conventional process. Preferably, the biologically active material subject to this invention has a lower propensity for adherence to other materials compared to the propensity for adherence of a biologically active material with the same, similar or larger particle size manufactured using a conventional process. Preferably, the biologically active material subject to this invention has increased uniformity compared to a biologically active material with the same, similar or larger particle size manufactured using a conventional process. Preferably, the biologically active material subject to this invention has reduced levels of dust compared to a biologically active material with the same, similar or larger particle size manufactured using a conventional process. Preferably, the biologically active material subject to this invention has improved rheology compared to a biologically active material with the same, similar or larger particle size manufactured using a conventional process. Preferably, the biologically active material subject to this invention has reduced segregation compared to a biologically active material with the same, similar or larger particle size manufactured using a conventional process. Preferably, the biologically active material subject to this invention has increased bulk density or tapped bulk density compared to a biologically active material with the same, similar or larger particle size manufactured using a conventional process. Preferably, the biologically active material subject to this invention has superior powder flow as defined by the Hausner ratio or Carr's index compared to a biologically active material with the same, similar or larger particle size manufactured using a conventional process. Preferably, the biologically active material subject to this invention has lower compressibility compared to a biologically active material with the same, similar or larger particle size manufactured using a conventional process. Preferably, the biologically active material subject to this invention has increased permeability compared to a biologically active material with the same, similar or larger particle size manufactured using a conventional process. Preferably, the biologically active material subject to this invention has a higher minium ignition energy compared to a biologically active material with the same, similar or larger particle size manufactured using a conventional process. Preferably, the biologically active material subject to this invention has higher hopper flow rates compared to a biologically active material with the same, similar or larger particle size manufactured using a conventional process. Preferably, the biologically active material subject to this invention has smaller critical orifice diameter compared to a biologically active material with the same, similar or larger particle size manufactured using a conventional process. Preferably, the biologically active material subject to this invention has smaller angle of repose compared to a biologically active material with the same, similar or larger particle size manufactured using a conventional process. Preferably, the biologically active material subject to this invention has smaller dynamic angle of repose compared to a biologically active material with the same, similar or larger particle size manufactured using a conventional process.

Problems solved by technology

Poor bioavailability is a significant problem encountered in the development of compositions in the therapeutic, cosmetic, agricultural and food industries, particularly those materials containing a biologically active material that is poorly soluble in water at physiological pH.
In addition, poorly soluble active agents tend to be disfavored or even unsafe for intravenous administration due to the risk of particles of agent blocking blood flow through capillaries.
The wet milling process, however, is prone to contamination, thereby leading to a bias in the pharmaceutical art against wet milling.
Many of these approaches commonly convert a drug into an amorphous state, which generally leads to a higher dissolution rate.
However, formulation approaches that result in the production of amorphous material are not common in commercial formulations due to concerns relating to stability and the potential for material to re-crystallize.
These techniques for preparing such pharmaceutical compositions tend to be complex.
By way of example, a principal technical difficulty encountered with emulsion polymerization is the removal of contaminants, such as unreacted monomers or initiators (which may have undesirable levels of toxicity), at the end of the manufacturing process.
However, these techniques suffer from a number of disadvantages including at least the inability to produce sufficiently small particles such as those obtained by milling, and the presence of co-solvents and / or contaminants such as toxic monomers which are difficult to remove, leading to expensive manufacturing processes.
Many of the technologies discussed above require the particles to be produced in a liquid suspension such that expensive and complicated further processing is needed to make common dry formulations such as tablets.
Some technologies such as micronization do produce material in a dry form, but the particles have inherently high cohesiveness and high static charge.
This leads to poor product flow and high aggregation properties.
The product fails to flow smoothly into containers (such as capsules) and aggregates significantly when poured.
It also adheres significantly to process equipment and containers, thus resulting in a significant loss of product.
One solution adopted by the prior art is to bind the material to a carrier product or to dissolve the material in a solution to improve product handling, but these steps add to the overall expense of any process.
Firstly, the nanoparticles produced by the Fukami process are sticky and difficult to handle.
Secondly, to overcome this problem the particles had to be dispersed in water and spray coated onto a carrier particle.
The spray coating process, which uses significant amounts of energy, is expensive and adds to the overall cost of the manufacturing.
One limitation of many of the prior art processes is that they are not suitable for commercial scale.
A component of this sub optimal bioavailability is also likely due to the poor water solubility of this drug.

Method used

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  • Method for the production of commercial nanoparticle and micro particle powders
  • Method for the production of commercial nanoparticle and micro particle powders
  • Method for the production of commercial nanoparticle and micro particle powders

Examples

Experimental program
Comparison scheme
Effect test

example 1

Spex Milling

[0335]A range of actives, matrices and surfactants in a variety of combinations were milled using the Spex mill. The details of these millings are shown in FIGS. 1A-1G together with the particle size distributions of actives that were milled.

[0336]These millings demonstrate that the addition of a small amount of surfactant to the milling matrix delivers a smaller particle size compared to millings of just an active and a single matrix. Some examples of this are samples Z and AA compared to sample Y; Sample AB compared to sample AC; sample AE compared to sample AD; sample AG compared to sample AF; sample AP compared to sample AO; sample AR compared to sample AQ, sample AT compared to sample AS; Samples AX, AY and AZ compared to sample AW; sample BC compared to sample BD; sample BI compared to BH; samples BL-BR compared to sample BK; samples CS-DB compared to sample DC. This last example is particularly noteworthy as these millings were undertaken at 45% v / v. This demonstr...

example 2

110 mL Attritor

[0341]A range of actives, matrices and surfactants in a variety of combinations were milled using the 110 ml stirred attritor mill. The details of these millings are shown in FIG. 2A together with the particle size distributions of actives that were milled.

[0342]These millings also demonstrate that the addition of a small amount of surfactant to the milling matrix delivers a smaller particle size compared to millings of just an active and a single matrix in a small scale stirred mill as well as the vibratory Spex mill. Sample F also demonstrates that small particles can be achieved at high % actives when a surfactant is present. Sample D and E also show that the addition of the surfactant also increased the yield of powder from the mill.

example 3

Second Matrix

[0343]In this example naproxen was milled with a mixture of two matrices using the Spex mill. The details of these millings are shown in FIG. 3A together with the particle size distributions of actives that were milled. Samples A and B were milled in a primary matrix of lactose monohydrate and 20% of second matrix. The particle size of these millings is smaller than the same milling with just lactose monohydrate (See example 1 sample No AH, FIG. 1B). The particle size is also smaller than naproxen milled in the secondary matrices (See example 1 sample No AI and AJ, FIG. 1B). This shows the mixed matrices have synergy together.

[0344]Samples C-E were milled in anhydrous lactose with 20% of a second matrix. All these samples had a particle size much smaller than naproxen milled in anhydrous lactose alone (See example 1 sample No AK, FIG. 1B).

[0345]These millings demonstrate that the addition of a second matrix to the primary milling matrix delivers a smaller particle size ...

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Abstract

The present invention relates to methods for producing nanoparticle and microparticle powders of a biologically active material which have improved powder handling properties making the powders suitable for commercial use using dry milling processes as well as compositions comprising such materials, medicaments produced using said biologically active materials in particulate form and/or compositions, and to methods of treatment of an animal, including man, using a therapeutically effective amount of said biologically active materials administered by way of said medicaments.

Description

FIELD OF THE INVENTION[0001]The present invention relates to methods for producing nanoparticle and microparticle powders of a biologically active material using dry milling processes, as well as compositions comprising such materials, medicaments produced using said biologically active materials in particulate form and / or compositions, and to methods of treatment of an animal, including man, using a therapeutically effective amount of said biologically active materials administered by way of said medicaments. Compositions of the present invention have unexpectedly improved powder handling properties relative to compositions made by conventional techniques, making them advantageous for use in commercial applications.BACKGROUND[0002]Poor bioavailability is a significant problem encountered in the development of compositions in the therapeutic, cosmetic, agricultural and food industries, particularly those materials containing a biologically active material that is poorly soluble in w...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): B02C19/00
CPCA01N25/12B02C19/0056A23L1/0029A61K9/0075A61K9/145A61K9/146A61K9/1617A61K9/1623A61K9/1635A61K9/1652A61K31/122A61K31/18A61K31/192A61K31/196A61K31/198A61K31/405A61K31/421A61K31/4709A61K31/497A61K31/53A61K31/5415A61K31/565A61K31/57A61K38/13A01N25/34A01N39/04A01N47/14A01N47/36A01N57/12A01N59/02A23P10/30A23P10/20A61P11/00A61P29/00A61P43/00A61K9/1682A01N37/38A01N55/02A01N57/20A23V2002/00A61J3/02A61K31/137A61K31/404A61K31/415A61K31/496A61K33/04A01N25/10B02C17/20A23L33/10A61K9/14A61K47/50A61K9/16
Inventor DODD, AARONMEISER, FELIXNORRET, MARCKRUSSELL, ADRIANBOSCH, H WILLIAM
Owner ICEUTICA PTY LTD
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