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93results about How to "Concentration maximization" patented technology

Sewage Treatment Process and System

A sewage treatment process is provided, which includes the following steps: a) sewage feeding step, comprising introducing raw sewage into a biological reaction tank (1) to a predetermined time or liquid level; b) reaction step comprising performing aeration and stirring intermittently in the biological reaction tank (1); c) treated water discharging step, comprising performing solid-liquid separation of the mixed liquor in the biological reaction tank (1) by a membrane separation device (2) to obtain a first permeate, which is taken as the final treated water; d) standby step comprising stopping aeration in the biological reaction tank (1); and e) phosphorus-enriched water discharging step, comprising keeping anaerobic condition in the biological reaction tank (1) and performing solid-liquid separation of the mixed liquor in the biological reaction tank (1) by a membrane separation device (2) to obtain a second permeate, the second permeate entering inside a phosphorus recycling unit (5) which is set independent from the biological reaction tank (1), the phosphorus recycling unit (5) removing phosphorus from water, the second permeate becoming low-phosphorus water, and the low-phosphorous water flowing back to the biological reaction tank (1); the sewage treatment process runs in cycle by repeating above steps. A corresponding treatment system is also provided.
Owner:SUN YOUFENG

Reflecting photonic concentrator

A linearly reflecting trough concentrator that receives spectral energy, preferably visible and near-infrared solar energy spectra, and linearly reflects that energy onto a smaller area on one side of the device, thereby concentrating the energy. The linearly reflecting trough concentrator has the geometry of a single slope-relief interval in a Fresnel lens, and in preferred embodiment comprises an array of heliostatic facets connected continuously to form the base of the trough, a non-imaging focal point where a photonic receiver is located, and a relief surface to connect the heliostatic array to the receiver location. When spectral energy enters the trough at an angle normal to the array's horizontal reference, the concentrator linearly reflects energy to one side of the device where an energy receiver is mounted. The concentrator comprises an array of heliostats oriented according to the negative profile of two interleaved linear Fresnel lens, where the slope of one is the relief of the other. The concentrator reflects energy above and to each side of the device. Optionally using a reflecting projector on one side of the device, energy is then doubly concentrated to the other side. The device offers higher concentration ratios with an equivalent trough depth than prior art reflective trough concentrators. The device requires less depth and offers a lower-profile than prior art reflecting concentrators with the same degree of concentration.
Owner:ASCENDANT ENERGY COMPANY

Intermittent reactor control system based on control variable parameterization method

The invention discloses an intermittent reactor control system based on a control variable parameterization method. The system comprises an intermittent reactor, and a temperature sensor, an analog to digital converter, a site bus network, a DCS (distributed control system), a main control chamber and product concentration status display which are arranged at the end of the intermittent reactor, and a digital to analog converter and a temperature control valve which are arranged at the end of the intermittent reactor. After duration of production process, initial concentration status of materials in the reactor and a target product required to increase concentration are determined by an engineer in a control chamber, the DCS acquires a temperature control strategy to enable the target product concentration to be maximum, converts the temperature control strategy into an open command for a temperature control valve, transmits the open command to the digital to analog converter at the end of the intermittent reactor through the site bus network, and enables the temperature control valve to act according to received control commands. The temperature sensor collects the temperature of the reactor in real-time and returns to the DCS to enable the engineer in the control chamber to master the production process timely. By the aid of the intermittent reactor control system, concentration of the target product can be maximized, and potential synergies are realized.
Owner:ZHEJIANG UNIV

Orthogonal collocation optimization based batch reactor control system

The invention discloses an orthogonal collocation optimization based batch reactor control system. The orthogonal collocation optimization based batch reactor control system comprises a batch reactor body, a temperature sensor at the end of the batch reactor body, an analog to digital converter, field bus networks, a DCS (distributed control system), a main control room temperature and product concentration state displayer, an analog to digital converter at the end of a temperature control valve and the temperature control valve. After an engineer in a control room specifies duration of a production process, initial concentration states of materials in the batch reactor body and a target product needing concentration increasing, the DCS executes an internal orthogonal collocation optimization method to compute a temperature control strategy enabling the concentration of the target product to be maximum, the temperature control strategy is converted into an opening instruction of the temperature control valve, and the opening instruction is sent to the analog to digital converter at the end of the temperature control valve through the field bus networks so as to enable the temperature control valve to act correspondingly according to a received control instruction. By the system, the concentration of the target product can be maximized, and potential tapping and efficiency improvement are realized.
Owner:ZHEJIANG UNIV

Method for concentrating aqueous containing solute into high concentration by hydraulic-membrane process under no difference in osmotic pressure

The present invention relates to a method of concentrating an aqueous solution at low pressure under a zero osmotic pressure difference condition, and more particularly, to a method of concentrating an aqueous solution containing a solute to be concentrated, at low pressure under a zero osmotic pressure difference condition. The method of the present invention comprises the steps of: (a) discharging water of a solute-containing aqueous solution to be concentrated, from a reverse osmosis separator to the outside, and transferring the concentrated aqueous solution to a zero osmotic pressure difference concentrator; (b) further concentrating the concentrated aqueous solution using the zero osmotic pressure difference concentrator comprising a feed chamber and a draw chamber, which are separated from each other by a reverse osmosis membrane or a forward osmosis membrane; and (c) recovering the solute and water from the aqueous solution further concentrated in the zero osmotic pressure difference concentrator. When the method of concentrating the aqueous solution at low pressure under the zero osmotic pressure difference condition is used, the aqueous solution can be concentrated to the maximum saturation concentration of a solute or a solution concentration of 100% using a reduced amount of energy without having to use an extraction solvent. In addition, there is an advantage in that a separate osmosis draw solution does not need to be used.
Owner:KOREA ADVANCED INST OF SCI & TECH

Batch reactor control system based on accurate punishment optimization

The invention discloses a batch reactor control system based on accurate punishment optimization. The batch reactor control system is formed by a batch reactor body, a temperature sensor at the end of the batch reactor body, an analog-digital converter, a field bus network, a DCS, a master-control room temperature and product concentration status displayer, a digital-analog converter at the end of a temperature control valve and the temperature control valve. After the duration time of the production process, the initial concentration state of materials in the reactor body and target products with concentration required to be improved are appointed by a control room engineer, the internal accurate punishment optimization method is implemented by the DCS, temperature control strategies which enable the concentration of the target products to be maximum are calculated and converted into opening instructions of the temperature control valve, the opening instructions are transmitted to the digital-analog converter at the end of the temperature control valve through the field bus network, and the temperature control valve executes corresponding motions. The temperature sensor at the end of the batch reactor body collects the temperature of the batch reactor body in real time, and therefore the control room engineer can master the production process at any time. The batch reactor control system enables the concentration of the target products to be maximum and achieves the aims of digging potential and improving efficiency.
Owner:ZHEJIANG UNIV

Optimal control system for piston flow tube reactor based on adaptive optimization control node

The invention discloses an optimal control system for a piston flow tube reactor based on an adaptive optimization control node. The system is composed of a piston flow tube reactor body, a liquid flow meter and a temperature sensor at the piston flow tube reactor end, an analog-to-digital converter, a field bus network, a DCS, a main control chamber coolant flow rate and reactor temperature display, a digital-to-analog converter at the flow control valve end, and a flow control valve. After the duration of the production process and the coolant flow rate control requirement are specified, theDCS obtains a flow rate control strategy and converts the flow rate control strategy into an opening instruction of the flow control valve, the opening instruction is sent through the field bus network to the digital-to-analog converter at the flow control valve end, the flow control valve correspondingly acts according to the received control instruction, the liquid flow meter and the temperature sensor collect the coolant flow rate and temperature of the piston flow tube reactor in real time and send the coolant flow rate and temperature back to the DCS. The concentration of a target product in a piston flow tube reactor can be maximized, and potential tapping and efficiency increasing can be achieved.
Owner:ZHEJIANG UNIV
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