Methods and systems for upgrading mixed pyrolysis oil to light aromatics over mixed metal oxide catalysts
US-2024010934-A1 · Jan 11, 2024 · US
US10052285B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10052285-B2 |
| Application number | US-201715407375-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 17, 2017 |
| Priority date | Nov 2, 2009 |
| Publication date | Aug 21, 2018 |
| Grant date | Aug 21, 2018 |
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Cryogranulation systems with improved dispenser assemblies are provided for use in manufacturing frozen pellets of pharmaceutical substances in a fluid medium. Methods of cryogranulating the pharmaceutical substance in the fluid medium are also provided. In particular embodiments, the dispenser assembly is used with suspensions or slurries of pharmaceutical compositions including biodegradable substances, such as proteins, peptides, and nucleic acids. In certain embodiments, the pharmaceutical substance can be adsorbed to any pharmaceutically acceptable carrier particles suitable for making pharmaceutical powders. In one embodiment, the pharmaceutical carrier can be, for example, diketopiperazine-based microparticles. The dispenser assembly improves the physical characteristics of the cryopellets formed and minimizes product loss during processing.
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The invention claimed is: 1. A method for cryogranulating a pharmaceutical composition, comprising: dispensing a pharmaceutical composition including diketopiperazine-based microparticles in a fluid medium into a flow of a cooling agent to produce, after interaction of the pharmaceutical composition with the cooling agent, pellets of the pharmaceutical composition, wherein dispensing the pharmaceutical composition includes dispensing a pharmaceutical suspension through a dispenser assembly into a flow of a cooling agent to form the frozen pellets, the dispenser assembly including first and second rows of dispenser ports, the rows of dispenser ports being disposed perpendicularly with respect to the flow of the cooling agent, wherein the dispenser ports of the first and second rows are angled with respect to vertical and wherein the dispenser ports of the first row are disposed at opposite angles with respect to the dispenser ports of the second row; and separating the pellets from the cooling agent. 2. A method for cryogranulating a pharmaceutical composition as defined in claim 1 , wherein 41% or more of the pellets have diameters greater than 4.75 mm. 3. A method for cryogranulating a pharmaceutical composition as defined in claim 1 , wherein 22% or less of the pellets have diameters less than 3.35 mm. 4. A method for cryogranulating a pharmaceutical composition as defined in claim 2 , wherein 22% or less of the pellets have diameters less than 3.35 mm. 5. A method for cryogranulating a pharmaceutical composition as defined in claim 1 , wherein the diketopiperazine-based microparticles comprise fumaryl diketopiperazine microparticles. 6. A method for cryogranulating a pharmaceutical composition as defined in claim 1 , wherein the diketopiperazine-based microparticles comprise fumaryl diketopiperazine microparticles loaded with a pharmaceutically active agent. 7. A method for cryogranulating a pharmaceutical composition as defined in claim 1 , wherein dispensing the pharmaceutical composition comprises supplying the pharmaceutical composition to an interior chamber of the dispenser assembly and dispensing the pharmaceutical composition from the interior chamber through the dispenser ports in the dispenser assembly. 8. A method for cryogranulating a pharmaceutical composition as defined in claim 7 , further comprising supplying nitrogen gas to the interior chamber of the dispenser assembly. 9. A method for cryogranulating a pharmaceutical composition as defined in claim 1 , wherein the pellets range in diameter from 3-6 mm. 10. A method for cryogranulating a pharmaceutical composition as defined in claim 1 , further comprising heating the pharmaceutical composition to prevent the pharmaceutical composition from freezing during dispensing.
Stationary reactors without moving elements inside (B01J19/08, B01J19/26 take precedence; with stationary particles B01J8/02) · CPC title
Organic compounds, e.g. phospholipids, fats · CPC title
in a liquid medium · CPC title
Devices or methods specially adapted for bringing pharmaceutical products into particular physical or administering forms · CPC title
Processes · CPC title
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