A system for biological decontamination uses high velocity low pressure emitters to create a fog of liquid decontamination agent or liquid and gaseous decontamination agents to blanket a volume to be decontaminated. The liquid decontamination agent and atomizing gas are suppled under pressure to the emitters which create various shock fronts in the gas stream as the gas is discharged from the emitters. The liquid decontamination agent is entrained in the gas stream as it is also discharged from the emitter, and the shock fronts atomize the liquid decontamination agent into droplets which form the decontaminating fog.

A mist blower with a Venturi housing for spraying water or chemicals onto objects such as livestock, orchards, weed areas or the like. The mist blower includes an air blower having an air discharge opening formed therein. A Venturi housing has its inner end in communication with the air discharge opening. An air discharge housing has its inner end embracing the outer end of the Venturi thereby creating a Venturi gap therebetween. The Venturi housing has a plurality of Venturi openings formed therein. As air is blown through the Venturi housing, the Venturi openings draw additional air into the air being discharged. As air is blown through the air discharge housing, additional air is drawn into the air discharge housing by way of the Venturi gap.

Initial liquid containing fine bubbles is produced by mixing water and air (step S11). Fine bubbles have diameters of less than 1 μm. The density of bubbles in the initial liquid is measured (step S13), and when the measured density is less than a target density (step S14), the initial liquid is heated and reduced in pressure so that the liquid is vaporized (step S15). As a volume of the liquid decreases, the density of fine bubbles increases, and high-density fine bubble-containing liquid is easily obtained. Alternatively, by increasing the density of fine bubbles in the initial liquid with using a filter that does not pass all fine bubbles, high-density fine bubble-containing liquid is easily acquired (step S15). When the density of bubbles in the initial liquid is greater than the target density, the initial liquid is diluted (step S16).

Ancillary embodiments and modifications to a homogenizer unit (“PPH”), and methods of use directed to purification of biogas or other raw methane streams. The apparatus includes a homogenizer body, one or more stream inlets (for the raw methane), one or more chilled water inlets, a mixing zone where the water stream is commingled with the raw methane stream, and a venturi immediately downstream from the mixing zone such that the commingled streams are pulled into the venturi resulting in homogenization. The PPH components are insulated to maintain the chilled water of the various streams at a cooled, below ambient temperature, increasing dissolution of the contaminant gases into the chilled water, and producing a purified methane stream including little or no H.sub.2S and CO.sub.2.

The present invention relates to a method of manufacturing spray-dried powders. During the process, a solvent is used. The process is done in multiple steps such that the emulsification mass ratio is low when removal of the solvent is started. Preferred solvents are isopropyl acetate and ethyl acetate. The invention also relates to a set-up to run the inventive process at industrial scale.

An embodiment gas treatment system (10) includes a gas treatment chamber (12). The gas treatment chamber (12) is separated into (i) a chemical agent chamber (14) adapted to store a liquid chemical agent and (ii) a gas/chemical agent mixing chamber (18) in fluid communication with the chemical agent chamber (14). The system (10) includes an atomising assembly (20) operatively associated with the gas/chemical agent mixing chamber (18) and a pressurised gas supply assembly (22) in operative fluid communication with the atomising assembly (20). The system also includes a chemical agent supply assembly (24) to provide fluid communication between the chemical agent chamber (14) and the atomising assembly (20) wherein the atomising assembly (20) is operatively adapted to atomise liquid chemical agent into a stream of pressurised gas fed from the pressurised gas supply assembly (22) into the gas/chemical mixing agent chamber (18).

An embodiment gas treatment system (10) includes a gas treatment chamber (12). The gas treatment chamber (12) is separated into (i) a chemical agent chamber (14) adapted to store a liquid chemical agent and (ii) a gas/chemical agent mixing chamber (18) in fluid communication with the chemical agent chamber (14). The system (10) includes an atomising assembly (20) operatively associated with the gas/chemical agent mixing chamber (18) and a pressurised gas supply assembly (22) in operative fluid communication with the atomising assembly (20). The system also includes a chemical agent supply assembly (24) to provide fluid communication between the chemical agent chamber (14) and the atomising assembly (20) wherein the atomising assembly (20) is operatively adapted to atomise liquid chemical agent into a stream of pressurised gas fed from the pressurised gas supply assembly (22) into the gas/chemical mixing agent chamber (18).

A spraying apparatus includes a spraying apparatus main body, a liquid introduction portion, a gas introduction portion, a gas-liquid spout portion, a liquid inlet, a gas inlet, a tubular flow passage, a spout, a flow passage having a taper, a straightener, and a projection portion. The liquid inlet allows a liquid flow to enter a gas-liquid mixer which is a space inside the annular gas introduction portion. The gas inlet allows a gas flow to enter the gas-liquid mixer. The straightener has an opening having an uneven shape provided in the flow passage having the taper. The projection portion is provided in the liquid introduction portion, protrudes to the gas-liquid mixer, and forms the straightener and a straightening outlet.

The present invention relates to a method of manufacturing spray-dried powders. During the process, a solvent is used. The process is done in multiple steps such that the emulsification mass ratio is low when removal of the solvent is started. Preferred solvents are isopropyl acetate and ethyl acetate. The invention also relates to a set-up to run the inventive process at industrial scale.

A nano-bubble water generating apparatus containing an application gas includes a motor, a pump integrated with the motor for supplying liquid, typically water, from an inlet pipe under a predetermined pressure through a supplying pipe to a pressure tank, a nano-bubble water generating tube mounted at the water entrance of a pressure tank, an electronic control portion, a pressure adjuster including an outer air inflowing portion to introduce an outer air or a specific gas supplied thereinto to control a pressure in the pressure tank, uniformly and a pressure adjusting portion airtightly coupled on the upper portion of the outer air inflowing portion to adjust an amount of outer air or specific gas to be supplied, and a nano-bubble water expanding tube for expanding and shattering nano-bubble water through an outlet pipe from the pressure tank, so that the size of the nano-bubble water is better micronized.