33results about How to "Recycling fit" patented technology

The invention discloses a floating automatic oil recovery device. The floating automatic oil recovery device comprises a fixed rack body, buoyancy tank bodies, at least one impeller, a speed reducer, a first driving unit, a second driving unit, a transmission assembly, an oil sucking assembly and a controller. The multiple buoyancy tank bodies are mounted on the fixed rack body. The impellers are mounted on the fixed rack body through a shaft lever. The floating automatic oil recovery device is simple in structure and reasonable in design; and by issuing a control instruction to the controller, the impellers can rotate, and then displacement of the whole device can be controlled. The overall using efficiency can be greatly improved while the basic function of floating oil recovery is achieved, and the device is quite suitable for recovery of large-area floating oil.

The invention discloses a tower type penetrating reverse flow fluidized direr. A material seal screw feeder is arranged at the upper portion of a drying tower. An air-lock valve discharger is arranged at the bottom of the drying tower. The upper portion of the drying tower is connected with an induced draft fan. The induced draft fan is connected with an evaporator of a heat pump system through a cyclone dust collector and then is evacuated. The evaporator of the heat pump system is connected with a host through a refrigerant pipe. The host is connected with a condenser through a refrigerant pipe. The air outlet end of an air blower is connected with the lower portion of the drying tower through the condenser. A plurality of layered repeated structures composed of sieve hole conical covers and sieve hole conical discs are arranged inside the drying tower. The sieve hole conical covers, the sieve hole conical discs, a discharging pipe, a stretchable vibration transmission shaft and a conical plug are arranged, so that penetrating, reverse flow, boiling and fluidization drying of materials are ingeniously and perfectly achieved, the classic boiling reverse flow drying mode is completely exceeded, more energy is saved, the drying quality is higher, and electricity consumption of the fans is lower; heat-pump-type tail heat recovery is particularly suitable for heat recovery at the low tail gas temperature.

The invention discloses a wastewater recycling system and a mixing station. The wastewater recycling system is used for the mixing station. The wastewater recycling system comprises a wastewater metering device, a material guiding device, a wastewater treatment device and a connecting pipe, wherein the wastewater metering device is arranged in a main body of the mixing station and is communicated with a mixing mainframe in the main body; the material guiding device is detachably arranged below the mixing mainframe and is used for exporting the wastewater in the mixing mainframe; a wastewater inlet of the wastewater treatment device is communicated with the material guiding device, and a wastewater outlet is connected with the wastewater metering device through the connecting pipe for drain the treated wastewater to the wastewater metering device; therefore, the wastewater recycling system disclosed by the invention not only is easy and convenient to disassemble and assemble, simple in structural design and relatively low in equipment cost, but also can improve an energy conservation and environmental protection index of site operation of a mobile mortar mixing station.

The invention discloses a method for extracting general flavone from sorrel shell waste residues through microwave refluxing. The method comprises the following specific steps of: 1, removing impurities from naturally-dried sorrel shells, smashing, sieving with a sieve of 40-60 meshes, and putting into a constant-temperature drying oven for drying sorrel shell powder for later use; and 2, uniformly fixing the powder treated in the step 1 with 30-60 percent of ethanol in the weight volume ratio of 1:25-1:50, performing reflux leaching at microwave power for 10-25 minutes, performing suction filtration to obtain a general flavone extracting solution, removing ethanol by rotationally evaporating, and performing vacuum drying to obtain a general flavone solid. The content of general flavone in a concentrated solution is measured with an aluminum chloride colorimetric method. According to measurement, the extraction ratio of general flavone is 95 percent, and the yield is 0.20 percent. The method has the advantages of quickness, high extraction ratio, environmental friendliness and nontoxicity by taking ethanol water as a solvent, simple equipment operation, small solvent using amount, easiness for recovering and suitability for expanded production in plants. The method has wide application prospects in medicines and foods.

The invention relates to a filtrate recovery system and a method. The filtrate recovery system comprises the following components which are sequentially arranged at the downstream of a separator: at least two first-stage filtrate switching tanks arranged in parallel, afirst-stage cooler, a ceramic membrane device, at least two second-stage filtrate switching tanks arranged in parallel, a second-stage cooler, a nanofiltration membrane deviceand arecycled water tank; a waste liquid outlet of the separator is connected with thefirst-stage filtrate switching tanks through a pipeline with a controlvalve;liquid outlets of the first-stage filtrate switching tanks are connected with the first-stage cooler; an outlet of the first-stage cooler is connected with the ceramic membrane device, a clearliquid outlet of the ceramic membrane device is connected with the second-stage filtrate switching tanks,liquid outlets of the second-stage filtrate switching tanks are connected with the second-stagecooler, an outlet of the second-stage cooler is connected with the nanofiltration membrane device, and a clear liquid outlet of the nanofiltration membrane device is communicated with the recycled water tank. By utilizing the switching tanks, the concentration of the filtrate is controlled to change from low to high in one cycle, themembraneflux is integrally improved, and the recovery of productparticles in the filtrate and the recovery and reuse of the filtrate are realized.

The invention discloses a soft partition board type through counter-flow drier. An air suction hood and an air inlet hood are arranged at two ends of a casing of the drier respectively, the air suction hood is connected with an induced draft fan, and the induced draft fan is emptied after being connected with an evaporator of a heat pump system through a cyclone dust collector; the evaporator of the heat pump system is connected with a main unit through a refrigerant pipe, and the main unit is connected with a condenser through a refrigerant pipe; an air outlet end of an air blower is connected with the air inlet cover through the condenser; multiple soft partition boards vertically arranged in the casing of the drier divide an upper casing body and a lower casing body into a plurality of units respectively; the soft partition boards press materials softly and block air currents completely, and material conveying is not influenced; axial flow fans are arranged in the units, the upper fans face downward and the lower fans face upward. Through counter-flow drying of materials is ingeniously realized through the induced draft fan, the soft partition boards and the axial flow fans, the drying efficiency is improved, the drying speed is increased, and the energy consumption is also reduced; heat pump type tail gas heat recovery is suitable for heat recovery of tail gas with a lower temperature efficiently and conveniently.

The invention discloses a method for extracting fucoxanthin from gulfweed, and belongs to the field of fucoxanthin extraction processes, and the method comprises the following steps: A1, pretreatment; A2, extraction; A3, solid-liquid separation; A4, concentrating; A5, separation and purification; and A6, reconcentration. The method for extracting fucoxanthin from sargassum is simple in operation process, low in cost and suitable for large-scale production, and the extraction effect can be guaranteed.