Extrusion processes drying

Solventless Extrusion Process. The solvendess process for making double-base propellants has been used ia the United States primarily for the manufacture of rocket propellant grains having web thickness from ca 1.35 to 15 cm and for thin-sheet mortar (M8) propellant. The process offers such advantages as minimal dimensional changes after extmsion, the elimination of the drying process, and better long-term baUistic uniformity because there is no loss of volatile solvent. The composition and properties of typical double-base solvent extmded rocket and mortar propellant are Hsted ia Table... 

Extrusion Processes. Polymer solutions are converted into fibers by extmsion. The dry-extmsion process, also called dry spinning, is primarily used for acetate and triacetate. In this operation, a solution of polymer in a volatile solvent is forced through a number of parallel orifices (spinneret) into a cabinet of warm air the fibers are formed by evaporation of the solvent. In wet extmsion, a polymer solution is forced through a spinneret into a Hquid that coagulates the filaments and removes the solvent. In melt extmsion, molten polymer is forced through a multihole die (pack) into air, which cools the strands into filaments. 

In many cases supports are shaped into simple cylinders (1-5 mm in diameter and 10-20 mm in length) in an extrusion process. The support powder is mixed with binders and water to form a paste that is forced through small holes of the desired size and shape. The paste should be sufficiently stiff such that the ribbon of extmded material maintains its shape during drying and shrinking. When dried, the material is cut or broken into pieces of the desired length. Extrusion is also applied to make ceramic monoliths such as those used in automotive exhaust catalysts and in DeNOx reactors. 

The products formed after heating dried P-carotene at 180°C for 2 hr in a sealed ampoule (SI) with air circulation (S2) stirring with starch and water (S3) and during extrusion process (S4) were isolated. - In all systems, 5,6-epoxy-P-carotene (trans and two cis isomers), 5,8-epoxy-P-carotene (trans and four cis isomers), and 5,6,5,6-diepoxy-P-carotene were identified, along with 5,6,5,8-diepoxy-P-carotene in systems S3 and S4. Later on, along with the epoxides previously found, 5 P-apocarotenals with 20 to 30 carbons, P-caroten-4-one, and 6 different P-carotene cis isomers were isolated in systems S3 and S4, whereas lower numbers of degradation products were found in the other systems. ... 

Purely thermal denaturation of proteins requires much longer times collagen in moist heat below 120 °C needs 30 min to denature (Meyer et ah, 2005), wheat glutens must be subjected to 200-215 °C of dry heat for 72 min (Friedman et ah, 1987), and as mentioned above, whey proteins require at least 50 °C and 30 min for texturization without the use of extrusion processing. 

In many cases drying operations are critical to the production of successful commercial catalysts. Close control of the drying process is necessary to achieve the proper distribution of the catalyst precursor within the pore structure of the support. Drying also influences the physical characteristics of the finished catalyst and the ease with which subsequent pelleting or extrusion processes may be carried out. 

The first task was to produce carriers from different recipes and in different shapes as shown schematically in Fig. 8. The raw materials diatomaceous earth, water and various binders are mixed to a paste, which is subsequently extruded through a shaped nozzle and cut off to wet pellets. The wet pellets are finally dried and heated in a furnace in an oxidising atmosphere (calcination). The nozzle geometry determines the cross section of the pellet (cf. Fig. 3) and the pellet length is controlled by adjusting the cut-off device. Important parameters in the extrusion process are the dry matter content and the viscosity of the paste. The pore volume distribution of the carriers is measured by Hg porosimetry, in which the penetration of Hg into the pores of the carrier is measured as a function of applied pressure, and the surface area is measured by the BET method, which is based on adsorption of nitrogen on the carrier surface [1]. 

The matrix used for the encapsulation of juice solids was a mixture of low DE maltodextrin (DE 10) and lactose. A typical formulation prior to cooking would be 23% water, 26% lactose and 51% maltodextrin. This material was cooked to the desired temperature (ca. 110 C), mixed with 85 Brix juice solids and optionally, peel oil, extruded, washed and dried. The extrusion process is essentially the same as used by Swisher (3), A product containing up to 40% juice solids may be produced via this process. This loading of juice solids is substantially greater than the 10-15% juice solids loading claimed by Barnes and Steinke ( 5 ). 

In brief, the extrusion process involved emulsification of orange peel oil into a melt of the ingredients described above. The molten products were then extruded under pressure through a die template into a chilled isopropyl alcohol bath. Subsequently, the products were broken into small, rod-shaped particles and dried to remove the alcohol. 

Cellulose Acetate and Triacetate Fibers. Polymer solutions arc convened into fibers by extrusion. The dry-extrusion process, also called dry spinning, is primarily used lor acelate and triacetate. 

The dry-extrusion process consists of four operations dissolution of the polymer in a volatile solvent filtration of the solution to remove insoluble matter extrusion of the solution to form libers and lubrication, yam formuliun. and packaging. 

The dried powder blend is pressed to desired shapes in hydraulic or mechanical presses. In special cases, a presintering followed by shaping to final form may be required. Large components and tools may require cold isostatic pressing followed by green forming. Rods and wires are formed by the extrusion process. 

Solid lipid nanoparticles can be converted to solid dosage forms by, for example, granulation, whereby the SLN dispersion is used as the granulating fluid, or as the wetting agent in the extrusion process, or by spray-drying or lyophilizing the SLN dispersion. 

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