The present invention provides a method and system for providing on-site electrical power to a fracturing operation, and an electrically powered fracturing system. Natural gas can be used to drive a turbine generator in the production of electrical power. A scalable, electrically powered fracturing fleet is provided to pump fluids for the fracturing operation, obviating the need for a constant supply of diesel fuel to the site and reducing the site footprint and infrastructure required for the fracturing operation, when compared with conventional systems.

The present invention provides a method and system for providing on-site electrical power to a fracturing operation, and an electrically powered fracturing system. Natural gas can be used to drive a turbine generator in the production of electrical power. A scalable, electrically powered fracturing fleet is provided to pump fluids for the fracturing operation, obviating the need for a constant supply of diesel fuel to the site and reducing the site footprint and infrastructure required for the fracturing operation, when compared with conventional systems.

The present invention provides a method and system for providing on-site electrical power to a fracturing operation, and an electrically powered fracturing system. Natural gas can be used to drive a turbine generator in the production of electrical power. A scalable, electrically powered fracturing fleet is provided to pump fluids for the fracturing operation, obviating the need for a constant supply of diesel fuel to the site and reducing the site footprint and infrastructure required for the fracturing operation, when compared with conventional systems.

A method of safely mixing a hydrocarbon with an oxidant is provided. The hydrocarbon and oxidant are saturated with a non-flammable liquid in pre-mix zones that are flooded with the non-flammable liquid and fluidly connected to a common mixing zone that is partially flooded with the non-flammable liquid. The saturated hydrocarbon and oxidant combine within the common mixing zone forming bubbles of a homogeneous gas mixture of hydrocarbon and oxidant, preferably in a ratio of hydrocarbon to oxidant that is outside of the flammability limit, that can exit the non-flammable liquid into a headspace where it can be retrieved for use in an oxidative reaction process such as oxidative dehydrogenation.

A micro puree machine including a housing, a power shaft, a bowl assembly and a platform. The power shaft extends from the housing. The bowl assembly including at least one locking bowl element. The platform includes at least one complementary locking platform element that is configured to engage the at least one locking bowl element such that rotation of the bowl assembly relative to the platform is prevented at times the bowl assembly is positioned thereon. The platform is rotatable from a first position to a second position relative to the housing such that the platform raises the bowl assembly towards the power shaft during the rotation of the bowl assembly and platform. The raising of the bowl assembly facilitates connection between the power shaft and a blade assembly that is positioned in a lid assembly on the bowl assembly.

A viscous fluid reaction apparatus is described. The viscous fluid reaction apparatus comprises a glass reaction vessel. The viscous fluid reaction apparatus further comprises a gas-tight inlet assembly and a gas-tight stirrer assembly. The gas-tight stirrer assembly comprises a stirrer opening adapter, a stirrer coupling comprising a stirrer shaft seal connected to the stirrer opening adapter, a stirrer shaft comprising one or more stirrer blades located at a blade end of the stirrer shaft, and a motor coupling connected to the stirrer shaft. The viscous fluid reaction apparatus further comprises a motor connected to the motor coupling. The stirrer shaft passes through the stirrer coupling and the stirrer opening adapter such that the stirrer blade(s) are disposed in the glass reaction vessel at a blade height and the stirrer shaft is configured to rotate without compromising a gas-tight seal formed by the stirrer shaft seal.

A viscous fluid reaction apparatus is described. The viscous fluid reaction apparatus comprises a glass reaction vessel. The viscous fluid reaction apparatus further comprises a gas-tight inlet assembly and a gas-tight stirrer assembly. The gas-tight stirrer assembly comprises a stirrer opening adapter, a stirrer coupling comprising a stirrer shaft seal connected to the stirrer opening adapter, a stirrer shaft comprising one or more stirrer blades located at a blade end of the stirrer shaft, and a motor coupling connected to the stirrer shaft. The viscous fluid reaction apparatus further comprises a motor connected to the motor coupling. The stirrer shaft passes through the stirrer coupling and the stirrer opening adapter such that the stirrer blade(s) are disposed in the glass reaction vessel at a blade height and the stirrer shaft is configured to rotate without compromising a gas-tight seal formed by the stirrer shaft seal.

The present invention relates to a system and process for a nutraceutical beverage compounding system and methods for the same. Provided is a customizable supplement beverage system and method for personalizing and operating the same to a particular user and optionally for operative tracking. Proposed additionally is an operative system for receiving and individually identifying a concentrate or supplement combinations, for mixing the same prior to a use, and for dispensing the same for use, and for tracking control factors relating to the same.

Providing a method for generating and releasing 1-MCP gas from a complex carrier through the use of a 1-MCP generator that enables the application of at least one physical, releasing force to a carrier complex and/or mixture comprising water and the carrier complex, or the interaction of steam with a carrier complex and/or mixture comprising water and the carrier complex, over a determined period of time.

The present invention provides a method and system for providing on-site electrical power to a fracturing operation, and an electrically powered fracturing system. Natural gas can be used to drive a turbine generator in the production of electrical power. A scalable, electrically powered fracturing fleet is provided to pump fluids for the fracturing operation, obviating the need for a constant supply of diesel fuel to the site and reducing the site footprint and infrastructure required for the fracturing operation, when compared with conventional systems. The treatment fluid can comprise a water-based fracturing fluid or a waterless liquefied petroleum gas (LPG) fracturing fluid.