42results about How to "Simplify the dehydration process" patented technology

The invention relates to a process for producing polyphenyl thioether, comprising the following steps of:, mixing hydrogenous sodium sulfide, lithium chloride and N-methyl pyrrolidone in the weight ratio of (20-25): (2-6): (70-80), co-boiling the mixture and inert gases at 150-210 DEG C for distilling and dehydrating; separating solvent by refining; respectively adding santochlor, solvent and lithium chloride in anhydrous sodium sulfide, separating after complete reaction to obtain polyphenylene sulfide; compositely washing the polyphenylene sulfide to obtain pure polyphenylene sulfide; and reclaiming the lithium chloride by filtering, reclaiming the solvent and flashly evaporating dimethylbenzene solution in a two-period mode and cooling and crystallizing. The invention has the advantages of low cost, simple process, excellent performance of synthetic resin and high solvent recovering rate.

The invention discloses a reclaiming system for condensation heat of flue gas during pressurized oxy-coal combustion, and belongs to the field of energy technology application and CO2 capture. In the technology, by utilizing the characteristic that the condensation temperature of flue gas moisture under high pressure is improved to about 200 DEG C, the condensation heat of the flue gas moisture heats condensation water of a steam turbine, the condensation process is performed in a high-pressure flue gas condenser, the flue gas generated during pressurized oxy-coal combustion enters the high-pressure flue gas condenser, steam in the flue gas is cooled and releases latent heat of vaporization to heat the condensation water of the steam turbine, and the discharged flue gas is continuously compressed and liquefied to fulfill the aim of capturing CO2. Through the technology, the condensation heat of the flue gas moisture is fully utilized, the smoke discharge loss is reduced, the output of the steam turbine is improved, the energy consumption for capturing the CO2 is reduced, and the thermal economy of the pressurized oxygen enriched combustion generating system is improved.

The invention discloses a sludge modified diaphragm compressed deep dehydration process and system. The process comprises the following steps: (1) metering sludge, and entering an elliptical cascade sludge pre-thickening system for thickening and dehydration; (2) enabling the thickened sludge to directly enter a sludge conditioning tank for conditioning, sequentially adding a conditioner a and a conditioner b to be uniformly stirred, and modifying the sludge; and (3) enabling the modified sludge to enter a special sludge compressed dehydration equipment system for performing deep compressed dehydration treatment, and enabling the finally obtained cake sludge to enter an outwards sludge transport system. The improved process is simple and convenient to operate, and the moisture content of the treated sludge is 60% or less. The invention further provides a sludge modified diaphragm compressed deep dehydration system. According to the system, the dehydration efficiency of a filter press can be improved, the sludge volume is reduced, the cost is reduced, the land utilization efficiency is improved, the low-cost goal of the sludge is achieved, and convenience is brought to subsequent resource treatment.

The invention relates to a crude oil dehydrating device combing an electric field and a centrifugal field, which consists of a shell, an electric field and centrifugal field integral structure, a motor, a pulley, a triangle leather belt, a dehydrating power supply device, an oil tank and a sewage tank. A centrifugal field structure consists of a hollow shaft, a liquid inlet pipe, a water outlet pipe, an oil outlet pipe, a sealed taper centrifugal cavity, an oil collector, a liquid distributor, a water collector, and sealing joints of the water outlet pipe, the oil outlet pipe and the liquid inlet pipe, wherein the hollow shaft is arranged in the vertical center of the shell; the liquid inlet pipe, the water outlet pipe and the oil outlet pipe are arranged in the hollow shaft; the sealed taper centrifugal cavity is arranged in the middle of the hollow shaft; the oil collector is arranged on the upper part in the hollow shaft; the liquid distributor is arranged in the middle of the hollow shaft; the water collector is arranged on the lower part of the hollow shaft; and the sealing joints are arranged on the upper part of the hollow shaft and do not rotate. An electric field structure consists of a disk-shaped electrode plate, the other disk-shaped electrode plate, moving electrodes and fixed electrodes, wherein the disk-shaped electrode plate is arranged between the oil collector and the liquid distributor; the other disk-shaped electrode plate is arranged on the centrifugal cavity and staggered with the electrode plate of the hollow shaft; the moving electrodes are arranged at both ends of the hollow shaft; and the fixed electrodes are arranged at the upper end and the lower end of the shell and correspondingly and movably contact the moving electrodes. The upper fixed electrode and the lower fixed electrode are connected with the dehydrating power supply device; and a motor pulley is connected with the pulley on the lower part of the hollow shaft through the.

The invention belongs to the field of toluene diisocynate production technology and relates to a dehydration method during the production process of toluene diisocynate. Toluenediamine and phosgene have cold light gasification reaction to obtain a mixture flow of carbamyl chloride, amidogen hydrochloride and hydrogen chloride; the mixture flow flows into a phosgenation reaction tower; carbamyl chloride and amidogen hydrochloride react to produce toluene diisocynate and the by-product hydrogen chloride; at the bottom of a hydrogen chloride rectifying tower, the mixture flow of amidogen and hydrogen chloride is divided into two parts, most of the mixture flow returns to the top of the phosgenation reaction tower and serves as the backflow, and the rest of the mixture flow enters into a drain sump containing activated carbon as the catalyst; water and phosgene in the mixture flow react to produce hydrogen chloride and carbon dioxide to remove water in the mixture flow under the function of the activated carbon catalyst; the dehydrated mixture flow enters into the bottom of the phosgenation reaction tower for further rectification and is discharged from the bottom of the phosgenation reaction tower for next step. The dehydration technology is simple and environmentally friendly, the cost is low, and the dehydration effect is excellent.

The invention discloses a sedimentation, classified reverse filtering and dewatering and dry stacking method for fine grained tailings. Total tailing pulp discharged from a concentration plant is concentrated and dewatered by a deep cone thickener, underflow flows to a high-frequency vibrating screen, coarse grained tailings on the screen slide to a funnel of a sealing-tape machine or a bucket ofa scraper, and the coarse grained tailings are conveyed to a sand pool of a gravity water filtering workshop by the sealing-tape machine or the scraper; a bottomed rectangular filtering sand tank is defined on the workshop floor by the coarse grained tailings in the sand pool with a grab machine, and concentrated underflow in a T-shaped sand bin is conveyed into the filtering sand tank; overflow of the T-shaped sand bin serves as back water; a coarse grained tailing mixture in the filtering sand tank is reversely loaded to the funnel of the sealing-tape machine or a dump truck by the scarper,conveyed to a tailing dry stacking yard or a backfill reclamation site and compacted layer by layer. The method is used for dry stacking, backfill reclamation or downhole filling of the fine grained tailings and infrastructure construction of tailing dewatering, equipment investment is reduced by 50%, energy consumption is reduced by 85%, efficiency is increased by 70%, cost is reduced by 60%, andoperation management is simple.

The invention relates to a coal preparation process, in particular to a floatation-cleaned-coal dehydration process and simultaneously relates to a set of equipment combination for realizing same. The dehydration process is characterized by comprising the following steps of: leading floatation cleaned coal to automatically flow into a settling and filtering centrifuge for dehydration or pumping the floatation cleaned coal into the settling and filtering centrifuge by using a pump for dehydration, wherein the dehydrated floatation cleaned coal is directly used as a final product; and leading centrifugate and filtrate of the settling and filtering centrifuge to return to the step of floatation feeding, namely participating in floatation operation again. The equipment combination is characterized by being provided with no filter press and no secondary floatation machine, and the settling and filtering centrifuge is used as only equipment for dehydrating the floatation cleaned cola. The process and the equipment combination, provided by the invention, are favorable for greatly saving construction cost and reducing maintaining expenses and product cost, not only can ensure that the moisture index of a floatation cleaned-coal product is qualified, but also can simultaneously ensure the uniformity of quality indexes, such as ash content and the like, of the floatation cleaned-coal product.

The invention discloses a thickened oil three-phase separator which is used for removing free water and reducing viscosity by adding thin oil and is used in oil fields and mine fields. The thickened oil three-phase separator is composed of an outer shell, a separation cavity, a gas-liquid pre-separation barrel, a liquid distributor, an inlet, a gas communication pipe, a gas outlet, a gas distribution bag, separation filler, a thin oil adding distributor, a thin oil distribution mouth, a chemical agent distributor, a chemical agent distribution mouth, an oil spilling weir plate, a water outlet, an oil outlet, an oil cavity, a thickened oil and thin oil mixer, and the like. A thin crude oil distributor and a thin oil distributor are arranged in the separator, and then thin oil is enabled to permeate into a certain position inside the separation cavity, and then the viscosity of thickened oil is reduced after the free water is removed. The chemical agent distributor and the chemical agent distribution mouth are arranged in the separator, chemical agents are enabled to permeate into a certain position inside the separation cavity, and chemical demulsification is carried out on the thickened oil after the free water is removed. The thickened oil and thin oil mixer is arranged at the position of the oil cavity of the oil outlet of the separator, mixing degree of the thickened oil and the thin oil is increased with methods such as a mechanical vibration method, and the thickened oil is enabled to be discharged out of the separator smoothly.

The invention provides a food air drying method. The food air drying method comprises the steps of a method for preparing an air drying quality guaranteeing auxiliary agent and a method for performingair drying, wherein the method for preparing the air drying quality guaranteeing auxiliary agent comprises the steps of taking fresh lemons, performing squeezing to obtain juice, removing residues, taking juice for standby application, crushing dried aromatic hydrocarbon containing plants to obtain powder, pouring the powder into the lemon juice, performing sufficient stirring while pouring the powder until the powder is viscous and does not have dry powder, so that the air drying quality guaranteeing auxiliary agent is prepared and placed in a sterilized sealed box namely that the quality guaranteeing auxiliary agent is loaded into the box; and the method for performing air drying comprises the steps of taking fresh air, performing dampness removal, ultraviolet irradiation and aseptic filtration so as to obtain clean air having temperature being 18-30 DEG C and humidity being 45-70%, introducing the clean air into an adjunct room, enabling the clean air to flow past the quality guaranteeing auxiliary agent to be injected into an air drying room, enabling the air to flow past the fruit and vegetable raw materials for air drying, and then discharging the air out of the air drying room. The air drying method disclosed by the invention can maintain the flavor of foods to the maximum extent, the foods can be really reduced, the working procedures are simple, the equipment is simple, batched production is easy to realize, and the air drying method is suitable for cooked foods or fresh foods.

The invention discloses a method used for improving waste active sludge dehydration performance through adding of bacterial broth. According to the method, aspergillus niger, Pseudomonas aeruginosa, Streptococcus thermophilus, and Rhodococcus rhodococcus are adopted, a fermentation culture solution is prepared from a waste molasses diluted solution and waste active sludge; the fermentation culturesolution is inoculated with the above four microbes respectively at certain ratios, fermentation is carried out for 2 to 5d at 25 to 35 DEG C 160-180r/min so as to obtain a composite bacterial broth;the composite bacterial broth is added into waste active sludge, stirring reaction is carried out for 4h, dehydration is carried out, and after conditioning, sludge water content is reduced to be lower than 50%. The bacterial broth is excellent in adaptability on temperature and pH value, and excellent in flocculation capability, dehydration effect is improved obviously; the method is simple; cost is low; sludge obtained through dehydration treatment can be taken as a plantation substrate or a microbial fertilizer; and sludge resource utilization is promoted.

The invention discloses a rotational flow coarse graining sedimentation dehydration device which comprises a coarse graining processor and a precipitator, wherein the coarse graining processor comprises a swirler; a liquid inlet, an overflow port and a bottom flow port are formed in the swirler; the overflow port and the bottom flow port are externally connected with an overflow pipe and a bottom flow pipe respectively; the tail ends of the overflow pipe and the bottom flow pipe are connected with each other to be connected with a mixing liquid pipe; the other end of the mixing liquid pipe is connected onto a precipitator. In addition, the invention further discloses a method of dehydration by utilizing the rotational flow coarse graining sedimentation dehydration device. The method comprises performing coarse graining treatment on oil-water mixing liquid and performing sedimentation on the oil-water mixing liquid subjected to the coarse graining treatment. According to the invention, three separation methods are integrated in a manner of having advantages and removing disadvantages; the dehydration method is simpler compared with a coarse grinding separation method, easier to control compared with a swirler separation method, and more efficient compared with a thermochemistry sedimentation method, so that the miniaturization of the dehydration device is ensured, the stability of production operation is met, the construction cost of a separation facility is reduced, and the operating cost is decreased.

A method of producing desiccated aerobic granules, comprising: (a) subjecting aerobic granules to a size selecting step; (b) subjecting the size selected aerobic granules from (a) to a dehydration step; (c) subjecting the dehydrated size selected aerobic granules from (b) to a drying step.

The invention provides a device system and method for continuously producing alkoxy propane, and the method comprises the following steps: carrying out condensation reaction on a raw material solution in a filler reaction extraction tower under the action of a solid acid catalyst, and then carrying out countercurrent contact on the raw material solution and an extraction agent to obtain an extraction phase; and carrying out azeotropic distillation on the extract phase in a product refining tower to obtain a target product. According to the method, modified solid acid is used as a catalyst and is matched with an extracting agent, in-situ separation and removal of byproduct water and promotion of right shift of balance are realized through countercurrent contact, the retention time is short, and the conversion per pass can be improved; besides, in the rectification process, due to the existence of the extraction agent, the product separation process is greatly simplified, the number of equipment and energy consumption are remarkably reduced, and the extraction agent is low in price, easy to obtain, capable of being directly recycled and reused, free of subsequent treatment, green and environmentally friendly and has great market competitive advantages.