36results about How to "Achieve energy efficiency" patented technology

An autonomous robot performs maintenance and repair activities in oil and gas wells, and in pipelines. The robot uses the well and pipeline fluids to provide most of the energy required for the its mobility, and to charge a turbine from which it may recharge batteries or power a motor for additional propulsion. A control system of associated systems controls the robot, enabling the robot to share plans and goals, situations, and solution processes with wells, pipelines, and external control systems. The control system includes decision aids in a series of knowledge bases that contain the expertise in appropriate fields to provide intelligent behavior to the control system. The intelligent behavior of the control system enables real time maintenance management of wells and pipelines, through actively collecting information, goal-driven system, reasoning at multiple levels, context sensitive communication, activity performing, and estimation of the operators' intent.

The invention discloses a biomass three-section type entrained flow bed gasification technology with the function of waste heat utilization, which relates to the technical field of energy chemical technology. The gasification technology is realized in a way that: carbon powder, pyrolysis gas and oxygen, which are generated after the biomass is pyrolyzed, enter an entrained flow bed to obtain synthetic gas through gasification, and the energy of the gasification waste heat is transferred to water by a heat exchanger of a gasifier, thereby producing superheated steam. The gasifier of the entrained flow bed is divided into a high-temperature entrained flow bed section, a high-temperature heat exchanger section and a low-temperature heat exchanger section, wherein the high-temperature entrained flow bed section adopts a dry ash extraction entrained flow bed gasification technology, and the temperature of the synthetic gas at the outlet is 1280-1320 DEG C; at the high-temperature heat exchanger section, the temperature of the synthetic gas at the inlet is 1280-1320 DEG C, the temperature at the outlet is 580-600 DEG C, a shock chamber and a high-temperature superheater are arranged in the high-temperature heat exchanger section, and the synthetic gas enters the shock chamber at the temperature of 1000-1100 DEG C and leaves at the temperature of 700-800 DEG C; and at the low-temperature heat exchanger section, the temperature of the synthetic gas at the inlet is 580-600 DEG C, the temperature of the synthetic gas at the outlet is 220-230 DEG C, and a low-temperature superheater and a coal economizer are arranged in the low-temperature heat exchanger section. The invention is used for high-efficiency gasification of biomass.

This invention relates to an energy source consumption metering system for cement production enterprise, which comprises a data acquisition part to gather power consumption parameter of production facilities for A / D conversion and output by percent format; a data transmission part to send data from acquisition part to superior computer for process; and a data process part to real-time display facility power consumption parameters, store data by integer-point format to create report, and send important data to the server for storage and user browsing according to user request. This invention is reliable, simple, and low cost.

A compute memory system can include a memory array and a controller that generates N-ary weighted (e.g., binary weighted) access pulses for a set of word lines during a single read operation. This multi-row read generates a charge on a bit line representing a word stored in a column of the memory array. The compute memory system further includes an embedded analog signal processor stage through which voltages from bit lines can be processed in the analog domain. Data is written into the memory array in a manner that stores words in columns instead of the traditional row configuration.

Improved processes are disclosed for obtaining discrete ethanol and at least one discrete product containing a higher boiling alcohol from an aqueous fermentation broth. In the processes a vaporous, azeotropic mixture is obtained from the fermentation broth through fractionation by distillation and is maintained at a temperature sufficient to effect dehydration without condensation of ethanol and the at least one higher alcohol. The dehydrated mixture of alcohols is further fractionated by distillation to provide a dehydrated, ethanol-rich product and a dehydrated, higher alcohol-rich product.

The invention discloses a road vehicle wheel structure and a method for loading loads of a wheel. The method for loading loads of the wheel comprises the steps that a supporting piece for connecting a car body with a wheel axle is arranged in the direction of vehicle loads W; a mechanics lever is hinged to the supporting piece to decompose a part of vehicle loads WG, and meanwhile the part of force is converted into tension FL or thrust Fy in the same direction as horizontal wheel thrust Fp1 through rotation of the mechanics lever. The novel approach is provided for improving the mechanical efficiency of a wheel system, and the great purpose that the energy efficiency of the vehicle can be saved by 30% or more is achieved.

The invention relates to a device making heat or refrigerating or providing healthy heat water making use of remaining heat of generator. It is composed of tail gas efferent of electrical generator, self-opening air door at the flue for fume discharged, electric fume valve connected with the tail gas efferent and pipe of tail gas utilization generator connected with it. The tail gas utilization generator enters the generator of lithium bromide absorbing central air condition whose trailing end connects with the flue for fume discharged out of the generator. Lithium bromide absorbing central air condition can be single-action or double-effect cold or warm watering trough; the generator can be provided with tail gas as its energy only by the pipe of tail gas utilization generator but also can be tail gas after burning direct combustion engine, that is, there are not only pipe of tail gas utilization generator but also heating structure by burning in the generator. The invention can not only make full use of energy of tail gas and remaining heat of the electrical generator so that it has high utilization ratio of tail gas and reduces consume of fuel to a large degree, but also reduce pollution to environment by tail gas.

The invention provides a control method for a counter-rotating movable blade adjustable axial flow fan which comprises a first fan unit and a second fan unit. The control method comprises the following steps: acquiring a first function between optimization target performance of a fan and working state parameters of the fan; acquiring a second function between comprehensive performance of the fan and comprehensive state parameters of the fan; obtaining an actual comprehensive state of the fan under a working condition according to the actual working state parameters of the fan under the working condition and the second function; judging whether the actual comprehensive state of the fan meets actual requirements or not, and adjusting the actual working state parameters of the fan until the comprehensive working state of the fan meets the actual requirements if the actual comprehensive state of the fan does not meet the actual requirements; obtaining actual performance of the fan according to the final actual working state parameters of the fan and the first function; judging whether the actual performance of the fan meets the optimal performance state of the fan or not, and adjusting the actual working state parameters of the fan until the actual performance of the fan meets the optimal performance state of the fan if the actual performance of the fan does not meet the optimal performance state of the fan.

The invention discloses a concentrating and phosphorus removing method for excess sludge. The method comprises the following steps: (1) taking appropriate excess sludge mixed liquor to be processed, and determining sludge concentration and the content of phosphorus in clear water; (2) putting the excess sludge to be processed and a mixed concentrating agent into a stirring device for stirring at the sped of 300-330r / min; after uniformly stirring, transferring to a concentrating machine for concentrating to obtain concentrated sludge with the concentration of 40-50g / L, wherein the content of phosphorus in the clear water drained after concentration is smaller than 1mg / L. Compared with the gravity concentration method, the concentrating and phosphorus removing method for the excess sludge has small occupied area and short time. Compared with a mechanical concentrating method, the occupied area is small, the price of drugs is low, and the operation is simple and fast. The content of phosphorus in the clear water drained after concentration is smaller than 1mg / L, and the clear water returning a processing system has a small influence on the phosphorus removal of an integral processing system.

The invention provides an environment-friendly water surface hydroelectric power plant which comprises iron tower supports, a water wheel supported to the tops of the iron tower supports through a water wheel centre shaft, a reduction box and an electric generator. The water wheel is evenly provided with a plurality of groove-type blades, the two ends of the water wheel centre shaft are supported to the tops of the corresponding iron tower supports through lifting mechanisms and move up and down to adjust the height of the water wheel, one end of the water wheel center shaft is connected with the input end of the reduction box through a crank type transmission device. According to the environment-friendly water surface hydroelectric power plant, the groove-type blades are adopted and are in holding type contact with water flow, stress is concentrated, the fluid potential energy can be received to the maximum degree, the rotation twisting force of the water wheel and the water wheel center shaft is increased, and the aims of energy conservation and efficiency improvement are achieved; in addition, the water wheel center shaft and the water wheel of the environment-friendly water surface hydroelectric power plant move up and down through the lifting mechanisms, the end of the water wheel center shaft outputs power through the crank type transmission device, normal transmission of power at different heights of the water wheel center shaft is guaranteed, impact damage of floating objects in a river on the blades during large waves and fast flow is avoided, and the electric generation capacity and the viability of the power plant under the extreme hydrologic condition are guaranteed.

The invention discloses a household energy storage device combined with an energy body of a vehicle, comprising an upper cover, a lower device housing, a circuit board, and a fixing frame. The upper cover is connected to the lower device housing through a rotating shaft, and the upper The cover can be opened upwards or downwards relative to the lower device housing; the lower device housing is provided with an accommodating cavity; the circuit main board is connected in the empty cavity; the circuit main board is provided with a conductive public end; The fixed frame is installed in the empty cavity and is located above the conductive public end; the fixed frame is provided with an elastic lock head and an elastic button, the elastic button is connected with the elastic lock head, and the elastic button controls the rebound of the elastic lock head; The housing of the lower device is provided with an energy input port and an energy output port; the energy input port and the energy output port are respectively connected with the main circuit board. The invention has the advantages of simple structure, convenient, reliable and safe charging.

The invention relates to an air induction flow gathering siphon discharging device for a rain belt of a natural venting cooling tower. Part of drenching water under the natural venting cooling tower is collected by a flow gathering device, the drenching water collected into the flow gathering device is fed into a frustum communicator and vortex eliminating communicators which are connected with the flow gathering device; the bottoms of the frustum communicator and the vortex eliminating communicators are connected with a hydraulic self-balance pipe collection network; outlet pipes of the hydraulic self-balance pipe collection network are connected with a siphon pool which directly supplies water for hydraulic users; drain water of the hydraulic users is returned back to a water pool by drain pipes; water in the water pool is fed into a circulation pump for boosting by a water inlet pipe of the circulation water pump; outlet water of the circulation water pump is fed into a cooler by a circulation cooling water supply pipe; outlet water of the cooler is fed into the natural venting cooling tower by a circulation cooling water inlet pipe; the frustum communicator is provided with a guide fan blade; the vortex eliminating communicators are provided with adjustable air induction guide plates. The natural venting cooling tower is subjected to air distributing optimization, the temperature of circulation water is reduced, waterhead of part of drenching water is used, effects are increased, energy is saved and the operation economy of a cold end system is improved.

A gasifier of biomass three-stage entrained flow bed using exhausted heat includes a high-temperature entrained flow bed, a high-temperature heat exchanger and a low-temperature heat exchanger. A quenching chamber and a high-temperature super-heater are arranged in the high-temperature heat exchanger. The temperature of synthetic inlet gas of the quenching chamber is ranged from 1000 to 1100 degrees centigrade. The temperature of synthetic outlet gas of the quenching chamber is ranged from 700 to 800 degrees centigrade. The inner wall of the low-temperature heat exchanger is equipped with optical tube film-type water cooled wall. A low-temperature super-heater and an economizer are arranged in the low-temperature heat exchanger. The gasification method of the gasifier of biomass three-stage entrained flow bed using exhausted heat involves that coal powder, pyrolysis gas and oxygen after biomass pyrolysis flow into the entrained flow bed through the burner to obtain synthetic gas by gasification, and exhausted heat of gasification is passed to water by the heat exchanger of the gasifier to obtain super-heat steam. High-temperature synthetic gas flows out from the gasifier after cooling.