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66results about "Crystallization conditions screening" patented technology

Preparation equipment and method for efficiently purifying ferrite for chemical reagent

The invention discloses preparation equipment and method for efficiently purifying ferrite for a chemical reagent. The invention belongs to the technical field of chemical equipment. The preparation equipment comprises a feeding cylinder, a first infusion pump, a reaction pot, a filter, a second infusion pump, a crystallizing tank, a third infusion pump, a conveying mechanism, an infusion liftingmechanism, a first temperature detector, a second temperature detector and a drum dryer, wherein the side wall of the bottom of the feeding cylinder is communicated with a liquid inlet pipe of a firstliquid pump; a liquid outlet pipe of the first liquid pump is connected to the upper portion of the side wall of the reaction pot, the first temperature detector is installed in the middle of the side wall of the reaction pot, a heater is arranged on the bottom face of the reaction pot, the side wall of the bottom of the reaction pot is communicated with the liquid inlet end of the filter, and the liquid outlet end of the filter is communicated with a liquid inlet pipe of the second liquid pump. The preparation equipment disclosed by the invention can avoid the influence of atmosphere on thecrystallization process and improve the product quality.
Owner:WENZHOU CHEM MATERIAL FACTORY

Online measurement device for crystal size and shape in high-solid-content crystallization process

The invention discloses an online measurement device for the size and shape of a crystal in a high-solid-content crystallization process. The online measurement device comprises a solution amplifier,a measurement device, a peristaltic pump, a crystallization kettle, a dilution device and a liquid storage tank, a crystal-containing solution is arranged in the crystallization kettle; the inner wallof the solution amplifier is smooth, one end is an amplification end, and the other end is a contraction end; the contraction end of the solution amplifier is communicated with one end of the liquidstorage tank and one end of the crystallization kettle; the amplification end of the solution amplifier is respectively communicated with the dilution device and the peristaltic pump; the peristalticpump is communicated with the other end of the crystallization kettle; the solution amplifier, the peristaltic pump and the crystallization kettle form a complete passage through a pipeline; a measuring instrument of the measuring device is arranged in the outer side of the solution amplifier and focuses on the solution in the amplification end of the solution amplifier; and at least one stop valve is mounted on each branch of the pipeline. According to the invention, measurement of a crystalline solution with solid content higher than 10% is realized; and the pipeline heat preservation and constant-temperature tank is designed, so that the problems of solution crystallization on the pipe wall and pipeline blockage are avoided.
Owner:QINGDAO UNIV OF SCI & TECH

A method for returning small crystal particles in the slurry discharged from a reaction crystallizer

The invention discloses a method for returning small crystal particles in the slurry discharged from a reaction crystallizer. The method includes the following steps: (1) The slurry discharged from the reaction crystallizer first enters a slurry storage tank, and then is sucked out by a venturi tube and fed from The clear liquid of the clear liquid circulation pump is mixed and diluted; (2) The diluted slurry enters the hydrocyclone for continuous separation of large and small crystal particles, and the large particles and a small part of the clear liquid are taken out as underflow and enter the product storage tank, and the small particles and Most of the clear liquid is discharged into the settling reflux tank as the top flow; (3) In the settling reflux tank, small crystal particles settle down and return to the reaction crystallizer to continue to grow; (4) Most of the supernatant in the settling reflux tank The liquid is pumped out by the clear liquid circulating pump as carrier fluid and diluent, and a small part goes to the water treatment unit. The method has low equipment investment, is easy to realize continuous operation, can effectively improve the particle size distribution of the product, and can simultaneously improve the utilization efficiency of the raw material liquid and avoid environmental pollution.
Owner:QINGDAO INST OF BIOENERGY & BIOPROCESS TECH CHINESE ACADEMY OF SCI +1

Method for inducing crystallization of chalcogenide phase change material and application thereof

The invention belongs to the field of microelectronics, and particularly relates to a method for inducing crystallization of a chalcogenide phase change material and application thereof, wherein specifically, a dielectric material is in interface contact with a chalcogenide phase change material, and the dielectric material is of an octahedral structure, and provides a crystal nucleus growth center for crystallization of the chalcogenide phase change material at the contact interface of the dielectric material and the chalcogenide phase-change material so as to induce accelerated crystallization of the phase-change material. The method is further applied to an existing phase change memory unit, so that the dielectric material structure of at least one dielectric material layer in all dielectric material layers in contact with the chalcogenide phase change material layer is of an octahedral structure. According to the invention, the dielectric material with an octahedral structure is in contact with the interface of the phase change material layer, the contact interface is inherent to a memory unit device and does not need to be additionally introduced, the influence on the whole semiconductor process is reduced to the minimum, and the phase change material is not optimized and modified in the design of the phase change memory unit, so that a series of other problems caused by optimization of the phase change material are avoided.
Owner:HUAZHONG UNIV OF SCI & TECH

MVR crystallization salification grain control system and control method

The invention provides an MVR crystallization salification grain control system and a control method. The system comprises a forced circulation pump, a crystallizer discharging pump, an elutriation circulating pump, a control system, a forced circulation heat exchanger, an Oslo crystallizer and an elutriation separator, wherein a circulating liquid outlet is connected with a heat exchange inlet, aheat exchange outlet is connected with a circulating liquid inlet, a crystallization material liquid outlet is connected with a crystallization material liquid inlet through the crystallizer discharging pump, an elutriation clear liquid outlet is connected with a elutriation clear liquid inlet, a mother solution outlet is further connected to a connecting pipeline of a circulating liquid outlet and the forced circulation pump and is connected with a mother solution inlet through the elutriation circulating pump, and the control system is connected with the forced circulation pump, the crystallizer discharging pump and the elutriation circulating pump, respectively. The crystallizer is of an Oslo structure, the elutriation separator is additionally arranged, and the grains are primarily screened in the crystallizer and are further elutriated and screened by virtue of the elutriation separator, so that the quality of the product is guaranteed.
Owner:JIANGSU RUISHENGHUA ENERGY TECH CO LTD

Granulation and crystallization device used in sodium metasilicate preparation process

The invention discloses a granulation and crystallization device used in a sodium metasilicate preparation process, and relates to the technical field of sodium metasilicate production equipment.The granulation and crystallization device comprises a crystallization tank, a discharging mechanism, a granulation and crystallization mechanism and a wall scraping mechanism, a motor is arranged at the top end of the crystallization tank, and a slag discharging pipe is arranged at the bottom end of the crystallization tank; a slag discharging valve is arranged on one side of the outer wall of the slag discharging pipe, and a cooling liquid inlet pipe, a stock solution feeding pipe and a seed crystal feeding pipe are arranged on one side of the outer wall of the crystallizing tank. By arranging the crystallizing tank, the crystallizing bin, the motor, the filter plate, the water suction cylinder, the water suction groove hole, the rotating shaft, the spiral blade, the first connecting rod, the stirring rod, the second connecting rod, the vertical scraper, the stock solution feeding pipe and the seed crystal feeding pipe, quick separation of crystallized particles can be achieved, and the working efficiency of sodium metasilicate crystallization is effectively improved.
Owner:高安市环瓷达釉料有限公司

Equipment and method for producing inorganic salt with solubility changing along with temperature through cooling crystallization

The invention discloses equipment for producing an inorganic salt with solubility changing along with temperature through cooling crystallization. The equipment comprises a nucleation controller, a first delivery pump, a crystal growth device, a heat preservation settler, a second delivery pump, a centrifugal machine and a vibration drying bed which are sequentially connected. The nucleation controller comprises a nucleation tank, a first circulating pipe, a condenser and a vacuum pump, wherein one end of the first circulating pipe is connected with the side wall of the nucleation tank; the other end of the first circulating pipe extends into the nucleation tank from the bottom end of the nucleation tank and is horn-mouth-shaped; one end of the first circulating pipe is higher than the other end; a feeding pipe is arranged at the lower end of the first circulating pipe outside the nucleation tank; the sectional area of the first circulating pipe is 3-7 times the sectional area of the feeding pipe; a discharging pipe is installed at the position close to the bottom end of the nucleation tank and connected with the crystal growth device through the first delivery pump; the top end ofthe nucleation tank is sequentially connected with the condenser and the vacuum pump; and the crystal growth device comprises at least two crystallizers which are sequentially connected.
Owner:尹博闻
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