14 results about "Trickle flow" patented technology

The utility model discloses a trickle bed type wastewater degradation device, which relates to the technical field of wastewater treatment equipment and is characterized in that uncharged or positively charged substances in wastewater are fully contacted with an anode electrode by improving the distribution of electrodes and the structure of a reactor, so that the reaction degradation effect is effectively improved; according to the scheme, the trickle bed type wastewater degradation device comprises an electrolytic bath body and a bath cover arranged on the electrolytic bath body, at least one electrolysis chamber and a water storage chamber are arranged in the electrolytic bath body, and wastewater treated by the electrolysis chamber overflows to the water storage chamber after being fully stored; the tank cover comprises a tank cover cavity, a first electrode mounting hole group is formed in the tank cover cavity, cathode electrodes and anode electrodes are sequentially and alternately arranged in the first electrode mounting hole group, and the cathode electrodes and the anode electrodes penetrate through the electrode mounting holes to extend into the electrolysis chamber; and a dripping hole is also formed in the mounting hole of the anode electrode.

The utility model discloses a trickle bed reactor convenient for liquid discharge of a distribution tank, the trickle bed reactor comprises the distribution tank and a trickle tube arranged at the bottom of the distribution tank, the bottom wall of the distribution tank is provided with a mounting hole, the mounting hole comprises a small-diameter part located at the lower part and a large-diameter part located above the small-diameter part, and a positioning step is arranged between the small-diameter part and the large-diameter part; a connecting ring is arranged at the upper end of the dripping pipe, the dripping pipe is used for being inserted into the mounting hole from top to bottom for mounting, and after the dripping pipe is mounted on the distribution groove, the connecting ring is in contact with the positioning step and fixed to the large-diameter part, and the connecting ring is completely located in the large-diameter part. The installation structure of the distribution groove and the trickle tube is simple, after the trickle tube is installed, the upper end of the trickle tube is completely located in the large-diameter part of the installation hole, and liquid cannot remain in the distribution groove and can be fully utilized.

The utility model relates to the technical field of chemical equipment, and mainly discloses a trickle bed reactor for continuously producing calcium chloride solution through reaction of hydrochloric acid and limestone, which comprises an upper cone, a barrel and an eccentric lower cone, an acid inlet pipe supporting grid is arranged below the acid inlet pipe to divide the area below the acid inlet pipe into a plurality of independent compartments, the concentration of hydrochloric acid in the compartments is high, the reaction speed is high, a pulse flow reaction area is formed, and acid liquid can be uniformly distributed; the area below the cells is low in hydrochloric acid concentration and is a trickling reaction area, so that full reaction of hydrochloric acid is facilitated; a limestone supporting grating is arranged between the barrel and the lower cone, and a discharging pipe and a hydraulic control discharging valve assembly are arranged at the bottom of the barrel; the reactor is provided with bottom, middle and top graded exhaust ports to reduce the gas flow rate in the reactor and reduce foam entrainment; the structure obviously improves the hydrochloric acid conversion rate and the reactor productivity, and is suitable for continuous industrial production.

The present application relates generally to methods and systems for delivering amendments like sulfate to a subsurface below a ground surface. In one embodiment a process comprises advancing a borehole from the ground surface to the subsurface below the ground surface wherein the borehole is advanced above a water table. The borehole is at least partially filled with a mixture comprising gypsum and a granular media. The borehole is then irrigated with water to at least partially dissolve the gypsum and to spread the dissolved gypsum to a desired treatment zone below the ground surface. The irrigating may comprise employing a gravity fed trickle flow using an irrigation line while the desired treatment zone may comprise one or more hydrocarbons.

This invention discloses a trickle bed device for synthesizing chloroethylene carbonate, comprising a constant temperature water bath and a trickle bed. The trickle bed is disposed on the upper part of the constant temperature water bath, and an adjustment component is fixedly connected to the upper part of the trickle bed to adjust the outflow of liquid. A liquid film thickness adjustment component is disposed below the adjustment component to adjust the thickness of the liquid film during the trickle process. A deceleration component is disposed above the adjustment component to decelerate the liquid flowing down from the top of the trickle bed. By setting the adjustment component, if too much liquid is accumulated by the deceleration component, the inflow of liquid from the upper part will be reduced, preventing the liquid passing through the adjustment component from being impacted by the liquid from the upper part, which would cause the liquid flow rate to be too fast. Moreover, the adjustment component drives the deceleration component to adjust the thickness of the liquid film, so that the liquid film reacts fully with chlorine gas.

Embodiments of the present disclosure provide a kind of trickle bed reactor load control method, device, equipment and storage medium.The method comprises: obtaining the current load target value of trickle bed reactor;According to the load target value, adjust the liquid phase feed flow of trickle bed reactor;Obtain the current liquid phase feed flow, design liquid phase feed flow and design gas phase feed flow of trickle bed reactor;According to current liquid phase feed flow, design liquid phase feed flow, design gas phase feed flow, determine the set value of the gas phase feed flow of trickle bed reactor;According to the set value of the gas phase feed flow of trickle bed reactor, adjust the gas phase feed flow of trickle bed reactor.In this way, when load is raised and lowered, liquid phase feed flow and gas phase feed flow can be adjusted synchronously, maintain the liquid holdup of reactor in allowable range, so that the reactor can automatically reach new steady state.

The invention discloses an atomic layer deposition device and method for trickle-assisted manufacturing. The atomic layer deposition device for trickle auxiliary manufacturing comprises a trickle auxiliary system, a reaction cavity, a precursor source system, a gas path system, a tail gas treatment system, a control system and a power supply system. The trickle auxiliary system can carry out trickle treatment on a precursor source entering the reaction cavity, so that the uniformity of airflow of the precursor source is ensured, the precursor source is in full contact with a deposition substrate, the increase of the grain size of film nucleation and the increase of the nucleation density are promoted, the conformality of film growth on a complex substrate is improved, and the production efficiency is improved. And high-efficiency controllable growth of a large-area, continuous, uniform and high-quality thin film is realized.

The present application relates generally to methods and systems for delivering amendments like sulfate to a subsurface below a ground surface. In one embodiment a process comprises advancing a borehole from the ground surface to the subsurface below the ground surface wherein the borehole is advanced above a water table. The borehole is at least partially filled with a mixture comprising gypsum and a granular media. The borehole is then irrigated with water to at least partially dissolve the gypsum and to spread the dissolved gypsum to a desired treatment zone below the ground surface. The irrigating may comprise employing a gravity fed trickle flow using an irrigation line while the desired treatment zone may comprise one or more hydrocarbons.

An electrolyzer system is provided with a plurality of separator-electrode assemblies (SEA). The SEAs include a negative electrode, a positive electrode, and a porous separator positioned therebetween. The electrodes and the separator, and thus the SEA overall, have a flow-through configuration enabling bulk liquid- and gas-phase reactants and products to flow therethrough. SEAs are positioned serially along a length of the electrolyzer, and thus bulk flow occurs through each SEA cell sequentially, in contrast to "flow-by" architectures where flow occurs in parallel through all cells simultaneously. Liquid- and gas-phase inlets provide the reactants such as H2, CO2, O2, etc. which are electrochemically converted to value products by the SEAs and concentrated for removal by product outlets. These electrolyzer systems generate value products such as H2O2; epoxides; C2+ alcohols, such as ethanol; syngas (CO + H2); etc. even at room temperature while avoiding the disadvantages associated with degradation-prone polymeric ion exchange membranes.

The utility model discloses a high liquid level distribution tank of a tubular trickle reactor, the tubular trickle reactor comprises a cylinder, a tube plate, a high liquid level distribution tank and an upper sealing head fixed at the upper end of the cylinder, the tube plate is fixed at the upper part of the cylinder, the high liquid level distribution tank is mounted on the tube plate, the upper end of the high liquid level distribution tank is provided with an opening, and the upper sealing head is fixed at the upper end of the cylinder. An opening of the high-liquid-level distribution groove extends to the middle of the top of the upper end socket, the cross section area of the opening of the high-liquid-level distribution groove is smaller than that of the bottom of the high-liquid-level distribution groove, and the high-liquid-level distribution groove is of a big-end-down structure. The large-end-down structure of the high-liquid-level distribution groove can make full use of the internal space of the upper sealing head, a higher liquid level can be achieved, and compared with a cylindrical structure, the high-liquid-level distribution groove can effectively reduce the loading risk and the control difficulty of the liquid level.

The application relates to the technical field of organic amine preparation, and discloses a method for preparing 1,6-hexanediamine by aminating 1,6-hexanediol. The method effectively improves the overall conversion rate of the raw material 1,6-hexanediol by optimizing the distribution of the circulating material, and avoids the further reaction of the target product and the intermediate product to generate amine with twelve or even eighteen carbon atoms, so that the selectivity of the hexanediamine and the conversion rate of the 1,6-hexanediol are further improved compared with the traditional method of mixing the circulating material and the 1,6-hexanediol together and feeding into a trickle bed reactor.

The utility model discloses a fixed trickle bed reactor capable of stabilizing trickle, which comprises a cylinder, an upper seal head arranged at the upper end of the cylinder and a lower seal head arranged at the lower end of the cylinder, a trickle distributor and a reaction tube are arranged in the cylinder from top to bottom, the trickle distributor is provided with a trickle tube, the trickle tube is in butt joint with the reaction tube, and the reaction tube is in butt joint with the trickle distributor. A liquid phase feeding pipe and a gas phase feeding pipe are arranged on the barrel or the upper sealing head, a closed cavity is formed by the upper sealing head, the barrel and the trickling distributor, and the fixed trickling bed reactor capable of stabilizing trickling further comprises a liquid level sensor used for detecting the liquid level of a liquid phase material in the closed cavity; the pressure sensor is used for detecting the air pressure in the closed cavity; one end of the pressure stabilizing pipe is communicated with the closed cavity, and the other end is connected with a pressure stabilizing gas source; and the regulating valve is mounted on the pressure stabilizing pipe. When the device is stopped or feeding is stopped, pressure stabilizing gas is conveyed to the closed cavity through the pressure stabilizing pipe, so that the air pressure in the closed cavity is kept, and stable dripping of residual materials in the stopping stage is achieved.

The utility model relates to the technical field, in particular to a self-cleaning small-grid drip box. According to the technical scheme, the filter box comprises a box bottom plate, a box body, an arc-shaped frame and a filter frame, a partition plate is arranged in the box body, the inner space of the box body is divided into an overflow area and a filter area through the partition plate, a water inlet is formed in the overflow area, the box bottom plate is arranged at the bottom end of the box body, and the filter frame is arranged in the box body. Communication holes are formed in the corresponding box bottom plate below the filtering area at equal intervals, a cross-shaped lacing wire support is arranged at an opening in the top end of each communication hole, the arc-shaped frame is arranged above the filtering area, an arc-shaped stainless steel net is clamped on the arc-shaped frame, and the filtering frame is inserted into the box bottom plate and located at the lowest position of the arc-shaped frame. Through the design of the arc-shaped stainless steel net self-cleaning structure and the overhead filter cotton, efficient filtration, automatic collection of impurities and anti-overflow guarantee are realized, and the filtration efficiency and the maintenance convenience are remarkably improved.

A trickle bed reactor, comprising a plurality of catalyst beds connected in series and progressively increasing in catalyst mass in a direction from upstream to downstream; and a plurality of heat exchangers, wherein each of the heat exchangers is located between two of the plurality of catalyst beds, and wherein each of the heat exchangers does not exchange heat with an outer surface of a vessel that contains any of the catalyst beds.