280 results about "Fluidized bed drying" patented technology

According to the gasification fine slag dewatering and drying method and system based on the fluidized bed dryer, gasification fine slag with high water content can be dewatered and dried, the energy utilization rate is high, and waste of water resources is little. The method comprises the following steps: 1) carrying out flash evaporation concentration, sedimentation and filtration dehydration on the coal gasification black water in the black water treatment unit; (2) gasified fine slag to be treated is fed into a fine slag preheater to be subjected to heat exchange with a heating medium; 3) carrying out heat exchange on the preheated gasified fine slag and the superheated steam in a fluidized bed dryer to obtain dried gasified fine slag and secondary steam; 4) feeding the secondary steam into a secondary steam dust removal unit for dust removal treatment, and then feeding the secondary steam into a fine slag preheater; (5) the secondary steam output by the fine slag preheater is fed into a steam preheater for heat exchange, and preheated secondary steam is obtained; (6) the preheated secondary steam is fed into a steam superheater to be subjected to superheating treatment, and superheated steam is obtained; and feeding the superheated steam into a fluidized bed dryer.

The invention discloses material fluidization drying equipment, which is used for fluidizing and drying materials by heating gas and comprises a fluidization drying unit, a heat exchange unit, a heat exchange unit, a heat exchange unit, a heat exchange unit, a heat exchange unit and a heat exchange unit, wherein the fluidization drying unit consists of a heat-insulating layer and a plurality of material conveying pipes arranged in the heat-insulating layer; each material conveying pipe is used for feeding independently, and the to-be-dried material runs downwards and is fluidized and dried by the ascending heating gas in the descending process; and the circulating feeding unit is arranged on the periphery of the heat preservation layer and used for feeding materials to the material conveying pipe and feeding the dried materials into the material conveying pipe again, and circulating drying is formed. The invention further discloses a material fluidized drying method. According to the equipment and the method disclosed by the invention, the heated fluidizing gas is used for drying the material; materials can be circularly and repeatedly dried through the circular feeding unit; mass and heat transfer of the materials can be enhanced through the fluidized drying unit, and the drying efficiency is effectively improved.

The utility model belongs to the technical field of solid waste treatment, and particularly relates to a fly ash harmless and resourceful treatment system. The harmless and recycling treatment system for the fly ash comprises a mixing and stirring unit, a fluidized bed drying and preheating unit, a dioxin catalytic cracking unit, a washing and desalting unit, an evaporative crystallization and salt production unit and a flue gas treatment unit, the mixing and stirring unit is used for stirring and mixing fly ash, a curing agent and a catalyst according to a set proportion; a gas outlet of the dioxin catalytic cracking unit is connected with a gas inlet of the fluidized bed preheating and drying unit, a gas outlet of the fluidized bed preheating and drying unit is connected with a gas inlet of the evaporative crystallization salt-making unit, and a gas outlet of the evaporative crystallization salt-making unit is connected with a gas inlet of the flue gas treatment unit. According to the utility model, the energy consumption is greatly reduced and the cost is saved while harmless and resourceful treatment of the fly ash is realized.

The invention relates to the technical field of fluidized beds, in particular to fluidized bed drying equipment which comprises an air inlet base, a drying tower cylinder and an exhaust tower top, the drying tower cylinder is installed between the air inlet base and the exhaust tower top in a communicating mode, the air inlet base is located below the exhaust tower top, and a material supporting ventilation disc is rotationally inserted into the drying tower cylinder. The material supporting ventilation disc is provided with a vertically-through ventilation hole, a movable ring frame is arranged below the material supporting ventilation disc, and the movable ring frame is inserted into the drying tower cylinder in a sliding mode. Materials can enter the concave cavity through rotation of the concentric air cylinder, hot air in the concentric air cylinder dries the materials in the concave plate through the air holes, water vapor generated by the materials entering the concave plate under the hot air enters the interlayer cavity from the exhaust holes to be directly discharged, and the influence of the water vapor on the materials above is reduced; and meanwhile, new hot air enters the space of the materials from the air holes with different layer heights, so that the drying degree of the materials is increased.

The utility model discloses a multilayer fluidized bed dryer which comprises a shell, a plurality of layers of air distribution plates are arranged in the shell, the air distribution plates are of a porous structure, partition plates are arranged on the upper surfaces of the air distribution plates to guide flow, and cooling pipelines are installed on the lower surfaces of the air distribution plates to adjust the temperature. A feeding hole is formed in the upper part of the shell, a high-temperature gas inlet is formed in the lower part of the shell, and wet materials and high-temperature gas flow reversely; an active regulation and control means is adopted, cooling pipelines are arranged on one or more bed layers, the temperature of the bed layers is autonomously regulated, and the conditions that the overall temperature field of a large dryer is difficult to regulate, and one or more bed layers are overheated or deviated to set working conditions are overcome; and meanwhile, the problem of equipment shutdown caused by material melting, air distribution plate blocking and bed blocking is solved, and the device is good in stability, capable of running for a long period and suitable for large-scale production.

The invention discloses a preparation method and application of magnesium glycinate granules, and relates to the technical field of magnesium glycinate granule preparation.The preparation method comprises the steps that povidone and polyvinyl alcohol are adopted as adhesives for wet granulation, the polyvinyl alcohol is prepared into slurry with the concentration of 10%, magnesium glycinate and povidone are put into a wet granulator to be evenly mixed, and the magnesium glycinate granules are obtained; and adding polyvinyl alcohol slurry with the concentration of 10% to prepare slurry, performing wet granulation, putting the prepared granules into a drying machine, performing boiling drying, and finishing the dried granules through a screen, thereby obtaining the finished product magnesium glycinate granules. By optimizing the use of the adhesive, the Maillard reaction of magnesium glycinate in the storage and shelf life is effectively avoided, the stability and appearance of the product are kept, and the quality and market competitiveness of the product are improved; by adopting the magnesium glycinate particles provided by the invention, the compressibility is obviously improved, the pressed tablets are high in strength, and the magnesium glycinate particles can be produced on a large scale.

The invention provides a traditional Chinese medicine granule fluidized bed drying uniformity online monitoring and improving method and device, relates to the field of traditional Chinese medicine preparation production and online quality control, and solves the technical problem of uniformity judgment deviation caused by single-bed data isolated monitoring. The method comprises the following steps: inputting secondary bed outlet particle spectral data into a spectral model to obtain a secondary bed predicted water content M2, and integrating temperature data of each bed, process parameters and the secondary bed predicted water content M2 to construct a database. And an input vector set is generated after preprocessing. And inputting the input vector set into a principal component analysis model, performing PCA dimension reduction on the input vector set, extracting main components, and inputting the main components into a Hotelling T-party monitoring model. And calculating a control limit based on multiple batches of historical qualified data, comparing the T-party statistical magnitude with the control limit to judge a drying uniformity grade, and outputting a corresponding regulation and control strategy according to the drying uniformity grade. The method is used in the production and on-line quality control process of the traditional Chinese medicine preparation.

The utility model relates to the technical field of fluidized bed drying machines, in particular to a fluidized bed drying machine which comprises a drying machine body, a spiral conveyor, a feeding box, a supporting shell, a screening barrel, a feeding port, a rotating mechanism and a smashing mechanism, the spiral conveyor is installed on the drying machine body, the feeding box is fixedly arranged on the spiral conveyor, and the supporting shell is arranged on the supporting shell. The spiral conveyor communicates with the dryer body and the feeding box, the supporting shell is arranged in the feeding box, a plurality of supporting columns are fixedly arranged between the supporting shell and the inner wall of the feeding box, the screening barrel is rotationally arranged between the supporting shell and the inner top wall of the feeding box, the feeding opening is formed in the inner top wall of the feeding box, and the rotating mechanism is arranged in the feeding box. The control mechanism is arranged on the supporting shell and used for controlling the screen barrel to rotate, the smashing mechanism is arranged on the supporting shell and used for smashing caked materials in the screen barrel, and through the technical scheme, the problem that the caked materials affect the drying efficiency in the drying process of the fluidized bed dryer in the related technology is solved.

The invention relates to the technical field of fluidized bed drying, in particular to an improved fluidized bed dryer and a drying process. The drying machine comprises a material bed and a transverse moving mechanism; the bottom of the material bed is connected with a vibration source and can ventilate and dry upwards from the bottom; the transverse moving mechanism comprises a driving part assembled at the bottom of the material bed and a plurality of transverse moving beams distributed in the conveying direction of the material bed, and the transverse moving beams are slidably installed on the material bed in the width direction of the material bed. The driving piece is used for intermittently and synchronously driving the plurality of transverse moving beams and driving the adjacent transverse moving beams to reversely slide in a reciprocating manner; a plurality of first brushes and a plurality of second brushes are detachably installed on each transverse moving beam in the length direction of the transverse moving beam. Through various auxiliary drying treatments on materials and cleaning of the bed surface, the drying uniformity and sufficiency of material finished products are guaranteed, the uniformity of material particle sizes is improved, the quality of the dried material finished products is guaranteed, and follow-up stable storage is facilitated.

The invention relates to the field of health supplements, and discloses a preparation method of cordyceps sinensis hypha powder rich in cubilose peptide and elastin peptide, which comprises the following steps: carrying out superfine grinding on the cordyceps sinensis hypha powder to obtain powder with the particle size of 10-50 microns; mixing the obtained cordyceps sinensis mycelium powder with cubilose peptide powder, elastin peptide, small molecule peptide of gadus and the like and cubilose acid to form mixed powder; carrying out wet granulation on the mixed powder, and adding 1%-3% of a binding agent to form the mixed powder; and carrying out fluidized bed drying on the granulated particles at the temperature of 60-80 DEG C to obtain dry particles with the water content of less than or equal to 7.0%. The stability of the nutrition powder is remarkably enhanced by adopting vacuum packaging and the aluminum foil composite bag, and external oxygen and moisture are effectively isolated. The packaging protects active ingredients such as cordycepin, protein peptide and the like in the nutrition powder, and prevents oxidation or wet decomposition, so that the shelf life is prolonged, and the efficacy of the product is maintained.

The invention discloses a small multifunctional integrated drying device, and relates to the technical field of industrial drying experiment equipment. The small multifunctional integrated drying device comprises a bottom plate, a vertical supporting plate is fixedly connected to the middle of the upper surface of the bottom plate, a fluidized bed drying chamber, a spray drying chamber, a main controller, a shared centrifugal fan and a shared electric heater are fixedly installed on the front face of the vertical supporting plate, and an air filter and an induced draft fan are fixedly installed on the upper surface of the bottom plate; a cyclone dust collector is fixedly installed on the back face of the vertical supporting plate, a three-way pipe is fixedly connected to the top of the shared electric heater, a fluidized bed feeder is fixedly installed on one side of the top of the fluidized bed drying chamber, and a supporting ring, an annular base, a motor, a fixing plate and an air pressure sensor are fixedly installed on the lower portion of the inner wall of the fluidized bed drying chamber. The system can integrate the fluidized bed function and the spray drying function, and energy-saving and efficient operation is achieved through the shared air path, the heat energy recovery system and the self-cleaning distribution plate.

The invention discloses a fluidized bed dryer with an automatic temperature adjusting function, and relates to the technical field of fluidized bed dryers, the fluidized bed dryer comprises a drying assembly for drying grains, the drying assembly automatically feeds and discharges the grains, and meanwhile, the heating uniformity of the grains during drying is guaranteed; a detection assembly for sealing the top of the drying assembly is detachably arranged at the upper end of the drying assembly, the detection assembly seals the drying assembly to avoid leakage of grains in the drying assembly, and the detection assembly automatically samples and detects the grains in the drying barrel; an air inlet assembly for ventilating the interior of the drying barrel is detachably arranged at the lower end of the drying assembly, the ventilation temperature on the air inlet assembly is automatically adjusted according to the drying degree of grains in the drying barrel, the highest utilization efficiency of heat is guaranteed, meanwhile, drying of the grains is affected by improper temperature, the drying efficiency of the grains is improved, energy is saved, and the energy-saving effect is achieved. And the grains are automatically dried.

The invention relates to the technical field of chemical production, and discloses a continuous production process and a production system of paraformaldehyde. The continuous production process of the paraformaldehyde comprises the following steps: feeding a low-concentration formaldehyde aqueous solution into a formaldehyde concentration tower for reduced-pressure flash evaporation to obtain a high-concentration formaldehyde aqueous solution; pumping the obtained high-concentration formaldehyde aqueous solution into a spray granulation tower for spray granulation to prepare a paraformaldehyde material; and feeding the obtained paraformaldehyde material into a fluidized bed dryer for fluidized drying to obtain a paraformaldehyde product. By adopting a specific combination mode of flash evaporation, spray drying and fluidized drying, the polymerization degree of the prepared paraformaldehyde product is 9-11, and the purity can reach 92-96 wt%. And in cooperation with heat preservation and flow rate control, the polymerization problem caused by too high local concentration of formaldehyde can be effectively avoided, and the continuous production mode can be well met.

The invention discloses drying detection sampling equipment for battery grade lithium carbonate production, and relates to the technical field of lithium carbonate production, the drying detection sampling equipment comprises a fluidized bed dryer, an output pipe, a first assembly, a second assembly and a third assembly, the output pipe is fixedly communicated with the fluidized bed dryer, and the second assembly is located in the middle of the first assembly; the third assembly is located below the first assembly. The first assembly is used for guaranteeing stable collection work of lithium carbonate samples during sampling detection; through simple and compact part combination, the sampling function is more optimized, random, equal-ratio and interval sampling can be effectively achieved, and the sampling analysis accuracy is improved; meanwhile, the situation that the transferred and collected material quantity is lower than the normal process requirement due to material adhesion can be effectively avoided, and the effectiveness and accuracy of later analysis are improved; in addition, the material flowability can be assisted to be known, and the problems of blockage and adhesion in the conveying process due to the fact that the material flowability is poor but is misjudged to be qualified are solved.

The invention relates to the technical field of health-care food, in particular to a method for preparing selenium-enriched yeast. The preparation method comprises the following steps: S1, preparing mixed powder; s2, preparing a paste; s3, standing and fermenting the obtained paste; s4, adding anhydrous alcohol into the obtained fermentation product, stirring, centrifuging, taking precipitate, and recycling supernate; s5, adding purified water into the obtained precipitate, adding silicon dioxide at the same time, performing uniform stirring, and then uniformly laying the mixture on a fluidized bed distribution plate for drying to prepare a dry powder finished product; according to the present invention, the flour is adopted as the carbon source, the bean powder is adopted as the nitrogen source, the simplest solid state fermentation mode is adopted, the fermentation time is short, the selenium-rich yeast can be prepared in a large scale, and the carbon and nitrogen sources are the cheap edible raw materials, and no other chemical components are added, such that the complex separation purification process is not required after the fermentation is completed; the food can be directly eaten only through simple fluidized bed drying, and is low in cost, safe and reliable.

The invention relates to the field of old asphalt regeneration, in particular to an old asphalt mixture regeneration device and a regeneration process thereof.The old asphalt mixture regeneration device comprises a storage device used for storing materials, a fluidized bed drying system, a roller drying system, a stirring main machine and a dust removal system; the fluidized bed drying system is used for drying and metering small-particle-size asphaltic sand and comprises a feeding hopper, a fluidized bed, a first metering device and a first smoke exhaust device. The material storage device comprises a stock bin, a material overturning mechanism arranged in the middle of the stock bin and used for lifting and overturning materials and a discharging mechanism arranged at the lower end of the stock bin, an air inlet and an air outlet are formed in the two opposite side walls of the stock bin respectively, a feeding port and a discharging port are formed in the stock bin, and the discharging port is communicated with the discharging mechanism; and hot air circulating systems are arranged on the air inlet and the air outlet. The technical problem that asphaltic sand is easy to accumulate and adhere is solved.

The utility model discloses a vibrating fluidized bed dryer, relates to the technical field of vibrating fluidized beds, and aims to solve the technical problem that the thickness of materials added into a drying cavity of the conventional vibrating fluidized bed dryer is inconvenient to control. A feeding port is formed in one side of the top of the vibrating fluidized bed body, a discharging port is formed in one side of the bottom of the vibrating fluidized bed body, a pore plate is arranged in a drying cavity of the vibrating fluidized bed body, and a thickness limiting structure is arranged at the position, located at the feeding port, in the drying cavity of the vibrating fluidized bed body. The thickness limiting structure comprises a first vertical plate, a second vertical plate and an electric push rod, the first vertical plate is arranged in the drying cavity of the vibrating fluidized bed main body, and the second vertical plate is arranged on the side, opposite to the feeding opening, of the first vertical plate in a sliding mode. The vibrating fluidized bed has the advantage that the thickness of materials in the drying cavity of the vibrating fluidized bed main body can be adjusted.

The invention discloses a rapid preparation method of a large-size CuSn / Nb combined blank with good interface matching. The rapid preparation method comprises the following steps: step 1, carrying out drying treatment on CuSn alloy powder by adopting a fluidized bed drying method to obtain dried CuSn alloy powder; 2, the dried CuSn alloy powder is subjected to electron beam selective melting forming, and a porous large-size CuSn alloy blank is obtained; 3, the prepared porous large-size CuSn alloy blank is subjected to surface treatment; and 4, an Nb rod is inserted into the treated porous large-size CuSn alloy blank, and a large-size CuSn / Nb combined blank with good interface matching is obtained. According to the rapid preparation method of the high-performance large-size CuSn / Nb combined blank with the good interface cooperation, the problems that a porous large-size CuSn alloy blank prepared in the prior art is low in compactness, poor in mechanical property, inaccurate in through hole positioning, serious in alloy waste in the preparation process and the like are solved.

The utility model relates to the technical field of vibrated fluidized bed dryers, and provides vibrated fluidized bed drying equipment for ammonium sulfate production, which comprises an equipment shell and a fluidized bed, the fluidized bed is arranged in the equipment shell, drying components are arranged on two sides of the equipment shell, and a material distribution component is arranged between the interior of the equipment shell and the fluidized bed. The vibration assembly is arranged outside the equipment shell, the feeding cover is fixed to the top in the equipment shell, a conveying belt is arranged in the equipment shell, and a plurality of scrapers are arranged on the surface of the conveying belt. According to the technical scheme, the problems that in the related technology, when to-be-dried ammonium sulfate is continuously added into the vibrated fluidized bed dryer, the ammonium sulfate is prone to being accumulated on the top of a fluidized bed, materials are accumulated, finally, the ammonium sulfate cannot be evenly heated, water in the ammonium sulfate deviates, and the drying effect and the production quality of the materials are reduced are solved.

The application discloses a kind of compound fertilizer with nitrogen fertilizer slow-release and biocontrol function and preparation method, it is related to microbial compound fertilizer field, including the following components: nitrogen source carrier, physical net trapping material, 3,4-dimethyl pyrazole phosphate, biocontrol component, binder.A kind of preparation method, including the following steps: after silanization modification treatment is carried out to attapulgite, with polyglutamic acid aqueous solution mixed reaction, obtain self-assembly gel;Bacillus subtilis is embedded and handled, rhamnolipid is pre-emulsified, chitosan oligosaccharide is crosslinked with boric acid treatment, and is blended;Nitrogen source carrier is heated to melt, add self-assembly gel, mix evenly;Temperature control, add 3,4-dimethyl pyrazole phosphate, and keep warm reaction;Cooling, add the blend obtained in step S200, binder, mix evenly;Extrusion granulation, after fluidized bed drying, slow-release coating is carried out, and the target compound fertilizer is obtained.The application makes disease control efficiency to improve to 89.2%, and blocks nitrosomonas AMO enzyme activity for 120 days.

A stable pharmaceutical composition for oral administration, comprising sitagliptin and dapagliflozin, wherein said active ingredients are substantially free of contact from each other. A process for the preparation of a stable pharmaceutical dosage form for oral administration, comprising: Step 1: Weigh sitagliptin hydrochloride monohydrate and Microcrystalline Cellulose and sieve; Step 2: Wet granulation Step 3: Drying the granules in fluid bed dryer; Step 4: Sizing the granules; Step 5: Weigh dapagliflozin base, lactose monohydrate, and sodium starch glycolate, premix them and sieve; Step 6: Mixing granules from step 4 with excipients from step 5; Step 7: Lubrication with magnesium stearate, and Step 8: Compression of the homogeneous powder obtained from step 7 under controlled humidity in mono-layer tablets in a rotary tabletting machine. An alternative process comprising the following steps: Step 1: Weigh sitagliptin hydrochloride monohydrate and Microcrystalline Cellulose and sieve; Step 2: Wet granulation Step 3: Drying the granules in fluid bed dryer; Step 4: Sizing the granules; Step 5: Weigh dapagliflozin base, lactose monohydrate, and hydroxypropylcellulose and sieve; Step 6: Dry granulation of second active ingredient and the intra-granular excipients of step 5 and mix; Step 7: Sizing the slugs or flakes obtained from step 6; Step 8: Pre-Mixing the granules from step 4 and step 7; Step 9: Weigh sodium starch glycolate and sieve; Step 10: Mixing; Step 11: Lubrication with magnesium stearate, and Step 12: Compression of the homogeneous powder obtained from step 11.

The utility model discloses a refining device and a refining system for ultra-clean polypropylene. The refining device comprises a slurry premixing tank, a washing container, a centrifugal filter, a solvent recovery tower, a reflux tank, a fluidized bed dryer and a gas-liquid separator. According to the device, materials and energy are fully recycled, ash such as metal substances and oligomer entrained by polypropylene powder can be effectively reduced, and even electrical-grade polypropylene can be obtained. According to the utility model, on the premise of obtaining a refined polypropylene product, environment-friendly, low-consumption and stable long-period operation can be realized.

The invention provides a production process of ivabradine hydrochloride tablets, which comprises the following steps: A) premixing lactose, maltodextrin, corn starch and ivabradine hydrochloride, adding purified water, and performing wet granulation; b) drying wet granules obtained by wet granulation in a fluidized bed, and then finishing the granules; and C) mixing the whole granules, magnesium stearate and colloidal silicon dioxide, tabletting and coating to obtain the magnesium stearate-colloidal silicon dioxide tablet. Compared with a production process in the prior art, the ivabradine hydrochloride tablet adopting a wet granulation process has the advantages of high stability, high efficiency and low impurity content. Meanwhile, the production process is simple.

The invention provides an arrangement for reducing static charge in a fluid bed dryer. The arrangement includes a hollow cylinder having an inner surface and an outer surface. The inner surface has a plurality of slotted projections formed radially at equal intervals along the axis of the hollow cylinder. The outer surface has an ionizing apparatus mounted on each of the slotted projections through a retention means. The arrangement further includes a pair of coupling means at both ends of the hollow cylinder for coupling the arrangement to the hot air supply duct of the fluid bed dryer. On applying a voltage, the ionizing apparatus, generate positive and negative ions into the hollow cylinder. The generated positive and negative ions are carried by the hot air to the sample drying unit of the fluid bed dryer for neutralizing the static charge generated during the drying of the sample.

The utility model relates to the technical field of fluidized beds, in particular to a fluidized bed drying device which comprises a fluidized bed and a drying box arranged on the outer side of the fluidized bed, an air distribution seat is fixedly installed at the bottom of the fluidized bed, an air distribution plate is fixedly arranged at the top of the air distribution seat, and a supporting seat is arranged below the air distribution seat. A vibration mechanism is arranged between the supporting seat and the air distribution seat, an exhaust port is fixedly formed in the top end of the outer side of the fluidized bed, a bin door is rotationally arranged at the bottom end of the outer side of the fluidized bed in a sealed mode, a feeding port is formed in the top of the fluidized bed, a conveying pipe is fixedly installed on the left side of the drying box, and a heating bin is formed in the drying box. A circulating fan and a heater are arranged in the heating bin, and the fluidized bed drying device is arranged, so that the situation that an air distribution plate is blocked is avoided through the structural design in a vibration mechanism, and continuous operation of a fluidized bed is facilitated.

The application discloses a spray drying micro-capsule granulation system and method with an internal fluidized bed, and relates to the technical field of micro-capsule spray granulation. The system comprises a granulation tower, an internal fluidized bed, a first detection unit, a state sensing unit, an external fluidized bed, a second detection unit, a numerical simulation unit and a control unit. The primary particles generated by the internal fluidized bed drying granulation tower form a semi-finished product, and the semi-finished product is dried by the external fluidized bed to obtain a finished product. The numerical model unit creates and updates a first-order numerical model of the internal fluidized bed and a second-order numerical model of the external fluidized bed. The control unit evaluates the credibility of the humidity of the semi-finished product through the first-order numerical model, adjusts the operation parameters of the external fluidized bed through the second-order numerical model, and updates the first-order numerical model based on the updated second-order numerical model after updating the second-order numerical model through the humidity of the finished product. The two-stage drying is realized in a cooperative and adaptive control mode, and the product quality stability and system robustness are effectively improved.

The invention provides a yang-warming, turbidity-clearing and weight-reducing composition and a preparation method thereof, and relates to the field of weight-reducing compositions. The traditional Chinese medicine composition comprises the following raw materials in parts by weight: 5-25 parts of unprocessed radix aconiti lateralis, 30-70 parts of gypsum, 10-25 parts of rhizoma anemarrhenae, 10-20 parts of cassia twig, 8-20 parts of honey-fried licorice root, 5-15 parts of glutinous rice, 20-30 parts of semen coicis, 10-20 parts of poria cocos and 5-20 parts of rhizoma atractylodis macrocephalae. The preparation method comprises the following steps: S1, slicing unprocessed radix aconiti carmichaeli, steaming for 8 hours with high-pressure steam at 120 DEG C, drying at 60 DEG C until the water content is less than 8%, crushing, and sieving with a 100-mesh sieve S2, drying gypsum, rhizoma anemarrhenae, cassia twig and honey-fried licorice root at 70-80 DEG C, crushing and sieving with a 100-mesh sieve; s3, adding 9-10 times of water into the glutinous rice, boiling until the glutinous rice is gelatinized, and filtering to obtain a colloid mixture; and S4, uniformly mixing the medicinal powder obtained in the step S2 with the colloid mixture according to a ratio of 1: 0.3, granulating with a 18-mesh sieve, and drying with a fluidized bed at 45-50 DEG C until the water content is less than or equal to 5% to obtain the composition. According to the composition provided by the invention, the gypsum and the rhizoma anemarrhenae clear stomach heat and inhibit appetite, and the radix aconiti carmichaeli and the cassia twig warm kidney yang to improve the basal metabolic rate, so that the disruption is reduced and the deficiency is reduced.

The invention relates to the technical field of garbage fly ash treatment, and provides a garbage fly ash washing treatment method and system.The garbage fly ash washing treatment method comprises the steps that fly ash washing liquid is evaporated to obtain concentrated feed liquid; the concentrated feed liquid enters an evaporation crystallizer to be evaporated and crystallized to obtain crystal slurry liquid; centrifugally separating the crystal slurry to obtain sodium chloride crystal salt; controlling the water-salt ratio to wash the sodium chloride crystal salt to obtain mother liquor; the water-salt ratio is the ratio of the mass of the washing water to the mass of the sodium chloride crystal salt; evaporating the mother liquor to obtain sodium chloride wet crystal salt; fluidizing and drying the sodium chloride wet crystallized salt to obtain a sodium chloride crystallized salt product; obtaining the purity of the sodium chloride crystal salt product, and determining the purity fluctuation; when the purity fluctuation of the sodium chloride crystal salt product exceeds a target fluctuation range, triggering to adjust the water-salt ratio, so that the purity fluctuation of the sodium chloride crystal salt product is within the target fluctuation range. According to the method and the system, the purity fluctuation of the sodium chloride crystal salt product is reduced to be within + / -1.2% from + / -2.5%.

The utility model discloses a fluidized bed dryer for drying ABS (Acrylonitrile Butadiene Styrene) resin, which comprises a dryer body, the dryer body is directly arranged on the ground, a grinding mechanism is arranged at the upper part in the dryer body, and the grinding mechanism comprises a grinding box, a grinding rod, a belt pulley, a splayed belt and a first motor, and a grinding box is fixedly mounted at the upper part of the interior of the dryer body. According to the fluidized bed dryer for drying the ABS resin, the pulverizing mechanism is arranged, before the resin is poured into the dryer to be dried, pulverizing is conducted once, convenience is provided for subsequent comprehensive drying, meanwhile, the reciprocating intermittent rotating mechanism is arranged, a stirring rod can intermittently rotate by 180 degrees in a reciprocating mode to stir the resin, and the drying efficiency is improved. In addition, a peculiar smell purification mechanism is arranged, peculiar smell generated after resin is dried is extracted through an exhaust fan, then the peculiar smell is purified and discharged, and a guarantee is provided for the body health of operators.

The utility model discloses a material distributing device of a food-grade fixed fluidized bed, which comprises a material distributing device main body, a feeding channel is arranged at the top end of the material distributing device main body, a discharging channel is arranged at the bottom end of the material distributing device main body, an impeller material distributing valve is arranged in the material distributing device main body, and the impeller material distributing valve comprises a material distributing rotor and an impeller arranged on the material distributing rotor. A driving device is arranged on the outer side of the distributing rotor. On the premise of an original fixed fluidized bed drying system, the high-speed rotating impeller distributing valve is additionally arranged at the feeding end, downward air generated by high-speed operation of an impeller of the impeller distributing valve is mixed with materials and then enters the fixed fluidized bed, the materials are prevented from being blocked in a concentrated mode, the air distributing plate is prevented from being blocked, the production process is optimized, and the operation efficiency is improved.