Abstract: An oscillating bubble reactor can include a stream inlet configured to receive a contaminated liquid stream, a reactant gas source, a serial venturi reactor (SVR), a micro-nano-bubble aerator (MNBA), and a treated stream outlet. The SVR can be connected downstream to the stream inlet and configured to receive the contaminated liquid stream. The SVR can include a set of serially connected constrictions alternating with pipe segments having a larger diameter than a smaller diameter of the constrictions. The MNBA can be in the stream inlet or the serial venturi reactor. The MNBA can be connected to the reactant gas source and configured to release reactant gas microbubbles, nanobubbles, or a combination thereof into the contaminated liquid stream from the reactant gas source. The treated stream outlet can be connected downstream to the serial venturi reactor.

Abstract: A production management system is configured to dynamically controlling inventory of a semiconductor product to prevent overstock and stockout. The production management system includes a production planning module including components containing data of demand forecast, and customer order. The production management system further includes a dynamic inventory control module including a dynamic inventory control simulation module and an inventory management system, wherein the dynamic inventory control simulation module is configured to adjust a target inventory if a current inventory is beyond a threshold multiplied by the target inventory for M number of review cycles.

Abstract: A production management system is configured to dynamically control inventory of a semiconductor product to prevent overstock and stockout. The production management system includes a production planning module including components containing data of demand forecast, and customer order. The production management system further includes a dynamic inventory control module including a dynamic inventory control simulation module and an inventory management system, wherein the inventory management system is configured to record real inventory data, and wherein the dynamic inventory control simulation module includes simulators for target inventory, future inventory, future shipment and semiconductor product production.

Abstract: The embodiments of the present invention fill the need of properly controlling product inventory of semiconductor chips by providing methods and systems of dynamic inventory control. The methods and systems timely modify parameters affecting inventory. The parameters may include target inventory, cycle time, wafer start, future inventory and future shipment. In addition, the methods and systems gather real-time customer demand forecast to assist in production planning and adjustment. Further, the methods and systems identify inventory control turning points dynamically to adjust production activities to prevent overstock and to prevent stockout.

Abstract: The embodiments of the present invention fill the need of properly controlling product inventory of semiconductor chips by providing methods and systems of dynamic inventory control. The methods and systems timely modify parameters affecting inventory. The parameters may include target inventory, cycle time, wafer start, future inventory and future shipment. In addition, the methods and systems gather real-time customer demand forecast to assist in production planning and adjustment. Further, the methods and systems identify inventory control turning points dynamically to adjust production activities to prevent overstock and to prevent stockout.

Abstract: A method for recovering valuable chemical products from heavy hydrocarbons such as tar sand or petroleum waste products is disclosed and described. Heavy hydrocarbons can be contacted with a fragmentation fluid which includes ozone and a solvent carrier. The fragmentation fluid can be provided at supercritical conditions. For example, supercritical CO2 can be an effective liquid solvent carrier for ozone. During contact with the fragmentation fluid, the heavy hydrocarbons are reduced in size to form a product mixture of chemical compounds. This product mixture typically includes chemical species which are more suitable than the original heavy hydrocarbons to commercial uses and/or further separation to provide useful starting materials for a wide variety of synthesis and industrial applications.

Abstract: A method for extracting hydrocarbons from sands can include: providing sands containing a hydrocarbon; mixing the hydrocarbon sands with water; heating the water before, during, or after being mixed with the hydrocarbon sands; increasing the pressure within a closed vessel containing the heated hydrocarbon and water mixture in the presence of gas or by injecting with gas; releasing the pressure of the heated hydrocarbon and water mixture in the vessel so as to create microbubbles from the dissolved gas in the water mixture; and collecting the hydrocarbon from the water. Optionally, the process is substantially devoid of adding caustic agents to the hydrocarbon and water mixture.

Abstract: Disclosed is a method and a system for measuring customer delivery service. A projected customer delivery date is generated. At least one projected output volume is determined based on the projected customer delivery date. At least one actual output volume is determined, and an accuracy of the projected customer delivery date is determined based on the at least one projected output volume and the at least one actual output volume.

Abstract: Disclosed is a method and a system for measuring customer delivery service. A projected customer delivery date is generated. At least one projected output volume is determined based on the projected customer delivery date. At least one actual output volume is determined, and an accuracy of the projected customer delivery date is determined based on the at least one projected output volume and the at least one actual output volume.

Abstract: A method for recovering valuable chemical products from heavy hydrocarbons such as tar sand or petroleum waste products is disclosed and described. Heavy hydrocarbons can be contacted with a fragmentation fluid which includes ozone and a solvent carrier. The fragmentation fluid can be provided at supercritical conditions. For example, supercritical CO2 can be an effective liquid solvent carrier for ozone. During contact with the fragmentation fluid, the heavy hydrocarbons are reduced in size to form a product mixture of chemical compounds. This product mixture typically includes chemical species which are more suitable than the original heavy hydrocarbons to commercial uses and/or further separation to provide useful starting materials for a wide variety of synthesis and industrial applications.

Abstract: A computer integrated manufacturing system executes a program process that performs a capacity planning method that allocates usage of a plurality of manufacturing elements of a manufacturing enterprise by major and minor apparatus, squeezing for overhead cost consideration, and site balance for maintain basic operation. The program process begins by receiving at least one fabrication forecast describing scheduling and types of product lots that are predicted to be fabricated within a first period of time by the manufacturing enterprise from at least one order management system of the manufacturing enterprise. Rolling statistics of products lots fabricated during a second period of time are retrieved from a data retention device of the computer integrated manufacturing system. Capacity planning for the allocation of the product lot predicted to be fabricated by the manufacturing elements is performed.