7results about How to "Efficient mass transfer" patented technology

The utility model discloses a high-concentration organic wastewater treatment device which comprises a tank body, the top end of the tank body is connected with a water inlet pipe through a rotary water distributor, and the interior of the tank body is divided into an electrolytic catalytic oxidation area, an anaerobic reaction area and a sediment backflow area from top to bottom; the electrolytic catalytic oxidation zone is provided with a plurality of titanium-based electrode plates which are arranged in parallel at intervals, a porous ceramic catalyst is filled between the titanium-based electrode plates, the anaerobic reaction zone is divided into a plurality of reaction chambers by a plurality of baffle plates, the adjacent baffle plates in the vertical direction deviate from each other, the bottoms of the baffle plates are provided with flow guide angles, and the flow guide angles are communicated with the reaction chambers. The reaction chamber is filled with a modified polyurethane biological filler; the precipitation reflux zone comprises an inclined tube precipitation layer and a conical sludge hopper, and the conical sludge hopper is connected with the head end of the anaerobic reaction zone through a gas stripping pipe. The high-concentration organic wastewater treatment device has the advantages of being compact in structure, high in high-concentration organic wastewater treatment efficiency and high in impact resistance.

The invention provides a method for recovering lithium from waste lithium iron phosphate black powder, which comprises the following steps: S1, heating, stirring and mixing ethylene glycol and ferric chloride hexahydrate to obtain a eutectic solvent; s2, adding waste lithium iron phosphate black powder into the eutectic solvent, and reacting to obtain reaction slurry; and S3, carrying out solid-liquid separation on the reaction slurry to obtain a lithium-containing leachate. According to the method, the lithium in the waste lithium iron phosphate black powder can be selectively leached, and the leaching rate of the lithium can be increased.

This invention discloses a method for treating ammonia-containing tail gas, relating to the field of ammonia-containing tail gas treatment. The method involves the ammonia-containing tail gas entering from the bottom of an acid washing tower and passing sequentially from bottom to top through a bottom washing liquid zone, a first packing zone, a second packing zone, a spray zone, and a demister for treatment. The spray zone uses atomizing nozzles to spray out a mixed washing liquid, controlling the pH value and conductivity of the washing liquid. Each atomizing nozzle includes a nozzle body, a first chamber, multiple diversion holes, a second chamber, and an outlet hole formed on the nozzle body and connected sequentially. The opening width of the diversion holes is smaller than the opening width of the outlet holes, and the width of the outlet holes increases along the axial direction. The orthographic projections of the diversion holes and the outlet holes on the end face of the nozzle body near the outlet hole do not intersect. This method can achieve efficient removal of ammonia from the tail gas even when the pH value of the washing liquid is high, resulting in a low acid mist value in the tail gas. It eliminates the need for a secondary water washing tower for treatment, thus reducing costs.

This invention relates to an apparatus and method for the efficient capture of iodine-containing exhaust gas, comprising a tower system, a gas supply system, an absorbent system, an exhaust gas detection system, and a control system. Iodine-containing exhaust gas enters from the bottom of the tower system via the gas supply system and flows upward within the tower. The absorbent system enters from the top of the tower system via a nozzle and flows downward. The two gases come into countercurrent contact within the tower. Sodium hydroxide in the absorbent reacts with iodine in the exhaust gas to form iodide, thus converting iodine from the gas phase to the liquid phase, achieving iodine absorption and capture. After absorption and capture, the exhaust gas passes through a demisting section to capture entrained droplets before being discharged from the top of the tower system. The exhaust gas detection system measures the concentration of iodine in the exhaust gas. This method enables efficient gas-liquid contact and mass transfer, and achieves constant-temperature circulation and composition control of the alkaline solution. Through optimized tower structure and control system, it achieves stable and efficient capture of iodine from iodine-containing exhaust gas, possessing good potential for scientific research verification and engineering scale-up.

The invention belongs to the technical field of organosilicon chemistry, and particularly discloses a method for preparing p-chloromethyl phenethyl triethoxy silane through continuous alcoholysis of a silane mixture. The method specifically comprises the following steps: preheating a mixed raw material consisting of p-chloromethyl phenethyl trichlorosilane and chloropropyl trichlorosilane, and continuously and reversely flowing the preheated mixed raw material and overheated ethanol steam into an effective-height packed tower reactor, so that a mixed silane liquid film and the ethanol steam are in full contact on the surface of packing to generate alcoholysis reaction; hydrogen chloride generated by the reaction is immediately entrained and moved out by ethanol steam, and a product is continuously extracted from the tower bottom and is rectified and purified. The non-catalytic continuous alcoholysis process has multiple remarkable advantages, the greenization and simplification of the production process are realized by thoroughly abandoning the catalyst and the acid-binding agent, and the generation amount of three wastes is extremely small.

The invention discloses a core-shell structure catalyst as well as a preparation method and application thereof, and belongs to the technical field of catalysts. The core-shell structure catalyst is successfully synthesized by regulating and controlling the core-shell chemical composition and crystallization conditions. In the preparation method, the utilization of the seed crystal inhibits the influence of the core skeleton characteristics on the shell layer, and the subsequent secondary growth induces to form a shell structure which grows mutually. The catalyst prepared by the invention takes the ZSM-5 zeolite with an acidic core site as a main component and the MCM-22 zeolite with a supercage structure as a structural basis, the ZSM-5 zeolite and the MCM-22 zeolite have a synergistic effect and respectively show excellent performance in dehydrogenation, oligomerization, cyclization reaction and carbon deposition resistance of methane, and compared with a traditional catalyst, the catalyst has the advantages that the catalyst has higher catalytic activity by constructing a heterogeneous molecular sieve core-shell structure and loading the metal Mo, and the catalyst has better application prospect. According to the catalyst, the benzene yield is obviously improved, the service life is prolonged, and the carbon deposition resistance is relatively high. The prepared core-shell structure catalyst not only serves MDA, but also can be expanded to other high-temperature acid catalytic reactions, and industrialization and process integration are promoted.

The application discloses a method for preparing L-ascorbyl fatty acid ester by using an enzyme and a product thereof, and comprises the following steps: (1) a one-step method is used to prepare a microarray carrier with a hydrophobic and mesoporous structure, free enzymes are dissolved in a PBS buffer solution, and the enzymes are fixed on the microarray carrier by using a multiple adsorption method and are freeze-dried, so that a lipase microarray is obtained, the immobilization amount of the lipase microarray is between 100-300 mg / g, and the activity is 80-180 U / g; (2) L-ascorbic acid and fatty acid are added into a reaction solvent, the L-ascorbic acid is dissolved by stirring for a certain period of time, then the lipase microarray obtained in the step (1) is added, and the esterification reaction is carried out by stirring for a period of time, nitrogen is combined and vacuum is extracted to remove water, so that a crude L-ascorbyl fatty acid ester product is obtained; and (3) the crude L-ascorbyl fatty acid ester product obtained in the step (2) is separated and purified, and high-purity L-ascorbyl fatty acid ester is obtained. The application has the advantages of high catalytic efficiency, strong fat-solubility and antioxidant property of the product, simple operation, green environmental protection, simple product separation, and suitability for scale-up production.