Patent classifications
B01F3/20
High efficiency powder dispersion and blend system and method for use in well completion operations
An improved system and method for fluidizing dry powder-based additives into downhole well operations utilizes a dried, low-volume air stream and an ejector nozzle in order to disperse the powders into a liquid stream. In an embodiment, the system can be placed on a powder blending trailer in order to convey additives directly from bulk transport bins into a liquid stream, through the use of an atmospheric pressure hydration tank fitted with a cyclone separator to ensure an even dispersal into the liquid stream.
SYSTEMS AND METHODS FOR PRODUCING MATERIALS SUITABLE FOR ADDITIVE MANUFACTURING USING A HYDRODYNAMIC CAVITATION APPARATUS
Provided in one implementation is a method that includes introducing a volume of raw material into a chamber of a cavitation machine. The raw material can include a mixture comprising a powder and a solvent. The powder can have a first average particle size in the raw material. The method includes applying a hydrodynamic cavitation process to the raw material to produce a product material. The powder can have a second average particle size, smaller than the first average particle size, in the product material. The method includes causing the product material to exit the cavitation chamber and drying the product material to remove the solvent. Apparatus employed to apply the method are also provided.
Method and device for producing a conversion product, in particular starch paste
A method for continuously producing a conversion product, in particular starch glue, fried starch, dissolved gelatin or protein glue, wherein a starch-containing and/or protein-containing, preferably powdery starting material, in particular flour, starch powder, cereal grains, coarse cereal meal, gelatin powder or gluten powder, is fed to a mixing chamber (2) and the starting material, preferably powder, descending in the mixing chamber (2) is subjected to a liquid heated to a processing temperature (T.sub.U) of at least 50 C. for converting the starting material into the conversion product, in particular to at least a gelatinization temperature of the starch-containing starting material, a protein-dissolving and/or denaturing temperature of the protein-containing starting material or a frying temperature, in the form of a pressure jet (7) and is thereby conveyed against a baffle (10) preferably formed by an inner wall of the mixing chamber or by an installation in the mixing chamber.
System and method for deaerating beverages
A method of producing a carbonated beverage comprising a blend of water and syrup having a predetermined final carbonation level. The method includes the steps of: introducing CO.sub.2 into a flowing stream of a product blend comprising water, syrup and dissolved oxygen, such that CO.sub.2 is dissolved in the product blend; deaerating the CO.sub.2-containing product blend by introducing the blend into a vented atmospheric vessel, the interior of which is at ambient pressure with a headspace maintained above the surface of the liquid within the vessel, whereby dissolved oxygen is released from the product blend and vented from the vessel; pumping the deaerated product blend from the vessel, wherein the deaerated blend includes dissolved CO.sub.2 at an intermediate carbonation level less than the final carbonation level; and carbonating the deaerated product blend to the final carbonation level downstream of the vented vessel to produce a carbonated beverage for subsequent packaging. A system for performing the method is also provided, as well as a method of producing a beverage using nitrogen deaeration.
Jet fuel thermal oxidation test equipment
Jet fuels' thermal oxidation characteristics are evaluated via the Standard Test Method for Thermal Stability of Aviation Turbine Fuels. This test method mimics the thermal stress conditions encountered by jet fuel in operation and is often carried out by laboratory devices, known as rigs. The rigs include a test section having a sleeve and a heater tube arranged therein. A pair of bus bars secure the test section to the rig and apply a current to the heater tube. The applied current heats the heater tube and subjects the sample jet fuels that are flowing in the volume between the sleeve and heater tube to high temperatures, which may produce thermal oxidation deposits on the heater tube. Heater tubes are difficult to install, however, and a gauge may be used to ensure accurate placement of the heater tube within the sleeve. In addition, the fuel sample must be prepared via an aeration process, and systems are disclosed for automating the aeration process such that the sample is prepared precisely according to the test standard. Moreover, the rig includes a pump system that moves the fuel sample through the test section, and a pump system is provided in a double syringe arrangement that optimizes fuel flow through the test section without fluctuation. Finally, the rigs include cooling systems for cooling the bus bars and maintaining an appropriate thermal profile within the heater tube, and cooling systems may be provided that independently control the temperature of each bus bar.
Method for producing a lignocellulose plastic composite material
A method for producing a lignocellulose plastic composite material, in particular a simpler and more cost-effective option for producing lignocellulose plastic composite materials. Thermoplastic particles and a mixture of water and lignocellulose-containing particles are supplied to a refiner, and the lignocellulose-containing particles are reduced to fibers in the refiner. The thermoplastic particles are supplied to the refiner in a melted or fused state, or are melted or fused in the refiner, so that the melted or fused thermoplastic particles and the lignocellulose-containing particles that are reduced to fibers form material composite particles in the refiner.
MULTI-USE BEVERAGE SYSTEM
Described herein is a beverage system that is configured to produce beverages having different characteristics, such as different levels of carbonation including producing substantially non-carbonated beverages and carbonated beverages with a single machine. The beverage system includes a beverage appliance and a beverage container. The beverage container includes a beverage material, which can include a flavoring ingredient for a target beverage. The beverage appliance is used to access the beverage material from the beverage container and produce the target beverage. The beverage appliance and beverage container are adaptable to produce the target beverage having any of a range of carbonation levels or other characteristics.
HIGH EFFICIENCY POWDER DISPERSION AND BLEND SYSTEM AND METHOD FOR USE IN WELL COMPLETION OPERATIONS
An improved system and method for fluidizing dry powder-based additives into downhole well operations utilizes a dried, low-volume air stream and an ejector nozzle in order to disperse the powders into a liquid stream. In an embodiment, the system can be placed on a powder blending trailer in order to convey additives directly from bulk transport bins into a liquid stream, through the use of an atmospheric pressure hydration tank fitted with a cyclone separator to ensure an even dispersal into the liquid stream.
APPARATUS FOR PRODUCING A PERSONALISED COSMETIC PRODUCT
A manufacturing apparatus including a first capsule containing a predetermined amount of a first formulation, and a second capsule containing a predetermined amount of a second formulation, the first and second capsules being distinct from each other; a receiving device configured to receive the first and second capsules; and a mixing machine configured to receive the receiving device equipped with the first and second capsules, and to mix the first and second formulations contained in the first and second capsules so as to obtain the cosmetic product.
CROSS-LINKED HA BEADS AND PROCESS FOR MAKING SAME
This disclosure provides a hyaluronic acid (HA) bead, a dermal filler having hyaluronic acid (HA) and a process for preparing the HA beads. The process includes combining an HA compound with sodium hydroxide, forming an HA solution, and injecting the HA solution into an oil solution, and forming an emulsion with HA beads. A cross-linking reagent is added and the mixture is stirred for 24 hours in room temperature, thereby forming cross-linked HA beads. The HA beads are cross-linked and adapted to dissolve in vivo upon contact with hyaluronidase.