45results about How to "Extend reaction residence time" patented technology

A photocatalytic reactor equipment with granular or fibrous semiconductor material as catalyst for continuously degradating toxic organic sewage is composed of optical reactor, filter, pump and buffering tank. Its advantages are easy recovery of catalyst, high reaction efficiency, high optical utilization rate, and high treating capacity.

The invention provides a reacting device. The device comprises a micro reactor (1) and a tubular reactor (2), the tubular reactor (2) is located at the downstream of the micro reactor (1) in the flowing direction of reacting fluid, and the tubular reactor (2) is in series connection with the micro reactor (1). According to the reacting device, reacting materials can enter into the tubular reactingdevice to conduct smoother reaction after the reacting materials are violently mixed in the micro reactor; the problem of constantly reducing caused by the action of micro channel walls when the reacting materials perform flowing reaction in the micro reactor is effectively solved, and the pressure of the reacting materials can be ensured or maintained to ensure that the reacting materials can flow for a longer distance under the same feeding pressure, so that the reaction residence time is longer, the mixing degree is fully improved and the reaction efficiency is improved.

The invention discloses a preparation method for a catalysis/adsorption material by taking kieselguhr as a carrier. The preparation method comprises the following steps of adding 15-20 parts of absolute ethyl alcohol into 1 part of purified kieselguhr, then adding 1-3 parts of a metal compound, 0.1-0.3 part of aluminum oxide, 0.1-0.3 part of glass fibers, 0.02-0.04 part of nitric acid and 5-7 parts of deionized water in sequence under magnetic stirring for mixing and stirring; performing centrifugal washing on obtained substances by the deionized water; and drying washed ore pulp at first, and then calcining the ore pulp, thus obtaining the catalysis/adsorption material. The catalysis/adsorption material prepared by the method disclosed by the invention can prolong the retention time of organic pollutants in a reactor by using the adsorption capacity of kieselguhr, and loaded metal oxide can generate a relatively good catalytic oxidation effect in a discharging process, so that the oxidization degree of organic pollutants is increased.

The invention provides a coal liquefaction method and device. The coal liquefaction method comprises the steps as follows: first liquefaction reaction is carried out on coal slurry and hydrogen to obtain a first liquefied product, wherein the first liquefied product comprises a first gas mixture and a first heavy product and the first gas mixture comprises a first liquefied light oil and a first gas product; a first heavy product in the first liquefied product is separated and second liquefaction reaction is carried out on the first heavy product and the hydrogen to obtain a second liquefied product; and before or during the second liquefaction reaction, the method also comprises the step of adding a first hydrogenation catalyst to the first heavy product. Through the method and the device provided by the invention, the conversion rate and the oil yield of coal can be improved, and meanwhile, the hydrogen consumption and the gas yield are reduced.

The invention discloses a water curtain type discharge plasma efficient treatment device for organic wastewater. The treatment device comprises a high voltage electrode and a grounding electrode which are respectively connected with the positive and negative electrodes of the plasma power source, and an outer medium tube and an inner medium tube which are sleeved together, between the outer medium tube and the inner medium tube is a water curtain discharge area; wherein the outer wall of the outer medium tube is provided with an annular overflow groove, the outer groove wall of the annular overflow groove is higher than the tube wall of the outer medium tube, the grounding electrode is arranged in the annular overflow groove, the high-voltage electrode is embedded in the inner medium tube, the lower end of the inner medium tube is sealed, the lower end of the outer medium tube is communicated with a lower water tank, and the upper end of the annular overflow groove is sealed and provided with an air inlet pipe. The device takes full advantage of the ozone generated by the discharge plasma. In the field of water treatment, the device has the advantages of stable and high performance, no secondary pollution, high speed, simple structure, strong practicability and the like, and has a relatively good application prospect.

A system for desulfurizing limestone in a circulating fluidized bed boiler on the basis of flow state reconstruction comprises a hearth, a conveying mechanism, a storage bin mechanism and a pipeline, wherein the conveying mechanism comprises a temporary storage bin, a mixer and a fan; a temporary storage feed port and an exhaust port are formed in the upper part of the temporary storage bin; the storage bin mechanism comprises a storage bin, a warehouse top dust collector, a through pipeline, an electric heater and a fan; the system further comprises an air separator communicated with an exhaust gas outlet of the hearth, a return feeder, an air chamber arranged at the bottom of the hearth and led into the hearth from a primary air duct, secondary air pipes distributed on the front wall and the rear wall of the hearth, an inlet valve set communicated with the secondary air pipes and used for desulfurizing limestone in the boiler, a tail flue arranged at the top of the separator, as well as a return feeder leg integrated with the separator; the inlet valve set is connected with the mixer through the pipeline; and the return feeder is connected with the bottom of the return feeder leg. The system has the advantages that the structure is simple, the separation efficiency is high, discharging is facilitated and the like.

The invention discloses a method for continuously preparing polyolefin, particularly continuously preparing a polyolefin elastomer or a mixture thereof, and polyolefin prepared therefrom. The pre-polymerization is carried out by using a kettle reactor in the preparation process, and has the function of increasing the viscosity of the reaction system to facilitate the subsequent operation of a screw reactor; the static mixing polymerization is carried out by using a static mixer in the preparation process, and is used for further increasing the viscosity of the system and prolonging the reaction residence time; and the extrusion polymerization is carried out by using a reactive screw extruder in the preparation process to achieve the polymerization reaction under a high conversion rate anda high viscosity. The preparation method can be suitable for a wide variety of polyolefin, and is particularly suitable for the preparation of the polyolefin elastomer or the mixture thereof.

The invention discloses a method for producing baking soda large in particle size .The method comprises the following steps that seed crystals are put into a reaction crystallizer; mother liquor is introduced into the reaction crystallizer till the liquor level reaches an alkali liquor circulating outlet, and the solid-to-liquor ratio in the reaction crystallizer is controlled to be (0.05-0.15):1; alkali liquor and carbon dioxide containing mixed gas are introduced into the reaction crystallizer for reacting, meanwhile, the mixed liquor in the reaction crystallizer is circulated to an alkali liquor circulating inlet from the alkali liquor circulating outlet, and an external circulating system is set up; under the action of the external circulating system, baking soda crystals obtained through reacting are suspended in the reaction crystallizer, upper-layer fine grains are discharged to a large production system, lower-layer baking soda crystal slurry is discharged, the discharged lower-layer baking soda crystal slurry is thickened, dried and separated, and the baking soda product large in particle size is obtained .Reacting and crystallizing are integrated, the large-particle baking soda product with the grain size ranging from 20 mesh to 60 mesh can be continuously prepared, cost is low, and technological operation is easy.

The invention discloses a pyrolysis device for processing desulfurization waste liquid in a partial oxidation environment. The pyrolysis device comprises a pressure-bearing housing, a jacket, an insulating layer and a refractory brick which are arranged from outside to inside and connected together, and a gas separation section I, a spray pyrolysis section II, a mixed flow pyrolysis section III, an inactive salt pyrolysis section IV and a pyrolysis salt chilling section V are communicated from top to bottom to treat the desulfurization waste liquid in the partial oxidation environment. The device adopts a segmental treatment mode, so that decomposition of aromatic compounds and organic matters in the desulfurization waste liquid is ensured in the partial oxidation environment, COD and sulfides in the generated wastewater are reduced, meanwhile, pyrolysis of the inactive salt in the desulfurization waste liquid in the reducing atmosphere is ensured; therefore, the pollution problem of the desulfurization waste liquid is thoroughly solved and effective components in the desulfurization waste liquid can be recycled.

The invention discloses a urea backmixing and pyrolysis apparatus applicable to a SCR denitration system and a pyrolysis method. The apparatus comprises a tower body; the tower body is provided with, from top to bottom, a combustion-supporting wind pipeline, an inlet variable-diameter section, a pyrolytic reaction section, an outlet variable-diameter section and an outlet pipeline; the pyrolytic reaction section is provided with a spray gun layer, a compensation wind pipeline layer and a gas flow equalizing plate from top to bottom; the number of the spray gun layer is at least one; and the spray gun layer is provided with a plurality of spray guns used for spraying an atomized urea solution, the plurality of spray guns are uniformly and radially distributed on the tower wall of the pyrolytic reaction section, and the spraying direction of each of the spray guns downwardly extending along the axial direction of the pyrolytic reaction section. According to the invention, the urea solution is mixed with combustion-supporting wind for primary pyrolysis and then with compensation wind for secondary pyrolysis, so the mixing degree of the urea solution and hot gas is promoted and generation of urea deposit and crystal is prevented; thus, the decomposition efficiency of the urea solution is improved.

The invention relates to the technical field of preparation of 2, 4-dinitroaniline, in particular to a method for preparing 2, 4-dinitroaniline by using a microreactor. The method comprises the following steps: (1) preparing equipment, namely preparing a preheater, the microreactor and two chromatographic pumps; (2) connecting reaction equipment, respectively connecting two chromatographic pumps with the preheater and the micro-reactor, then connecting the preheater with the micro-reactor, and putting the preheater and the microreactor into a constant-temperature oil bath after the connectionis completed; (3) conveying a reaction material, namely conveying ammonia water to the preheater at a preset flow rate, conveying the molten 2, 4-dinitrochlorobenzene to the microreactor at a preset flow rate, and mixing and reacting with the ammonia water to obtain 2, 4-dinitroaniline; and (4) after the reaction of the material in the step (3) is completed, preparing the redundant ammonia gas into ammonia water again for reuse through an ammonia gas recovery device, and continuing to reuse the ammonia generated by the reaction of ammonium chloride generated by the reaction and potassium hydroxide. Tthe method has the characteristics of high production efficiency, low energy consumption, economy, environmental protection, safety and reliability.

The invention discloses a solid waste gasification system and a gasification method thereof. At present, solid waste disposal is mainly based on incineration, which is likely to cause secondary environmental pollution. The air distribution mechanism is arranged at the bottom of the furnace body of the present invention; the primary air inlet of the air distribution mechanism communicates with the gasification fan through the one-way mixer, and the secondary air inlet communicates with the inner cavity of the furnace body through the annular air duct, and also communicates with the outlet of the one-way mixer. The tuyere; the mixed steam inlet of the one-way mixer is connected with the high-temperature steam outlet; the furnace body is divided into an upper space layer, a drying chamber, a dry distillation chamber, a lower space layer, a reduction chamber, an oxidation chamber and ash chamber; the drying chamber layout and the high-temperature steam inlet Connected dry steam nozzles, retort steam nozzles connected to the high-temperature steam inlet in the retort chamber; high-temperature steam coils are arranged in the dry chamber and retort chamber, connected to the high-temperature steam inlet and high-temperature steam outlet; Arrange the reducing gas outlet in layers. The invention continuously transforms solid waste into combustible gas and high-temperature sintered and solidified slag to achieve harmlessness.

The invention belongs to the technical field of catalysts, and particularly relates to a size-adjustable palladium-based catalyst limited by carbon nanotubes as well as a preparation method and an application of the size-adjustable palladium-based catalyst. By improving the whole process flow and the reaction conditions and parameters (such as types and proportions of reaction raw materials, reactant concentration and reaction temperature) of all key process steps, precious metal active substances are limited in the inner cavity of the carbon nano tube, and the metal size can be regulated andcontrolled by controlling the reaction conditions. The preparation method is simple in process, convenient to operate, cheap and easily available in reaction materials, and capable of preparing the confinement catalyst with specific catalytic performance according to specific requirements, including a carbon nano tube confinement palladium monatomic catalyst and a carbon nano tube confinement palladium cluster catalyst, so that accurate regulation and control between the loading capacity and the size are realized. The prepared palladium-based catalyst can be used for catalyzing a reduction reaction of an aromatic nitro compound and shows excellent catalytic activity.

The invention provides a denitrification device for coking wastewater mixed liquid and a method for improving denitrification ability of coking wastewater. The device comprises an anaerobic tank, an anoxic tank, an aerobic tank and a settling tank which communicate with one another successively, wherein a good carbon source case and a carbon-source-free case are arranged in the anoxic tank; the good carbon source case is arranged at a water outlet end of the anoxic tank; the carbon-source-free case is arranged at a raw water and mixed liquid inlet end of the anoxic tank; and the good carbon source case is in half isolation from the carbon-source-free case. The denitrification device has the beneficial effects that the total nitrogen of water drained from an A/O system is greatly reduced, treatment load of rear denitrification is greatly reduced, therefore, reaction retention time of rear denitrification is reduced, and the investment and the running cost are reduced; and meanwhile, alkalinity produced by high denitrification efficiency is improved, consumption of alkali liquor for nitrification of an aerator tank can be reduced, the running cost of the aerator tank is reduced, and therefore, the denitrification device is dual-purpose.

The multi-nozzle gasification furnace comprises a hollow furnace body, a reaction chamber, a radiation waste boiler chamber and a chilling chamber are sequentially arranged in the furnace body from top to bottom, the reaction chamber is communicated with the radiation waste boiler chamber through a gas-slag channel, a downcomer is arranged at the lower end of the radiation waste boiler chamber, and the chilling chamber is communicated with the reaction chamber through a gas-slag channel. The lower end of the descending pipe extends into the chilling chamber; a plurality of main burners are arranged on the outer side wall of the reaction chamber, and an ignition start-up burner and a plurality of auxiliary burners are arranged at the top of the reaction chamber. The invention further provides a using method of the multi-nozzle gasification furnace with the top auxiliary burner. According to the multi-nozzle gasification furnace with the top auxiliary burner and the application of the multi-nozzle gasification furnace, the reaction retention time is prolonged, the carbon conversion rate of the gasification furnace is increased, the energy consumption is greatly reduced, the operation cost is reduced, and the requirement for environmental protection is met.

The invention discloses a method for preparing 2, 4-D acid by chlorinating phenoxyacetic acid by using a micro-reaction device. The method comprises the steps: dissolving phenoxyacetic acid in glacialacetic acid to obtain a glacial acetic acid solution of phenoxyacetic acid, and pumping the glacial acetic acid solution of phenoxyacetic acid into a pre-cooling pipe 1 of the micro-reaction device for pre-cooling; pumping a sodium hypochlorite solution into a pre-cooling pipe 2 of the micro-reaction device for pre-cooling; then pumping the two solutions into a micro-mixer in the micro-reaction device to be fully mixed; introducing the mixed solution into a micro-reactor of the micro-reaction device for reaction; after the reaction is finished, carrying out post-treatment on the reaction solution to obtain the 2, 4-D acid. The preparation method of the 2, 4-D acid can overcome the problems that an expensive solvent and a complex catalyst need to be used, many byproducts are produced and the like in the existing 2, 4-D acid post-chlorination technology, the continuous degree of the production process is high, the safety of the production process can be greatly improved, and the yield of the product is increased.

The invention discloses a dry-wet combined sulphur removal system for waste incineration flue gas. The dry-wet combined sulphur removal system for the waste incineration flue gas belongs to the technical field of flue gas desulfurizationenvironment protection, and comprises a cooling tower, an absorption tower, a bag-type dust collector and a chimney connected sequentially, wherein a water atomization spray head is arranged on the top part of the cooling tower; a flue gas inlet is formed in the top part of the cooling tower; a flue gas outlet is formed in the bottom part of the cooling tower; an activated carboninjection pipe and a powderyslaked lime injection pipe are arranged on a gas flue for connecting the cooling tower and the absorption tower; the absorption tower is connected with a quick limeserous fluid inlet pipe; the quick limeserous fluid inlet pipe is connected with a quick limeserous fluidbatching system. After the waste incineration flue gas passes through the dry-wet combined sulphur removal system provided by the invention, the smoke dust is reduced to be around 30mg/m<3>, the HCl is reduced to be around 50mg/m<3>, and the SOX is reduced to be around 200mg/m<3>.

The invention provides an in-furnace desulfurization method of a circulating fluidized bed boiler, which comprises the steps of introducing a desulfurizing agent and fire coal into a furnace body of the circulating fluidized bed boiler, allowing to react, feeding a superfine composite additive into the circulating fluidized bed boiler from a secondary air hole of the circulating fluidized bed boiler, and carrying out in-furnace desulfurization. The method of the invention combines the in-furnace desulfurizing agent and a superfine composite additive spraying technique, so that super-low emission of SO2 can be stably achieved. The problems are solved that, for instance, traditional wet and semi-dry desulfurization processes have large coverage, secondary pollution is caused, water resourceconsumption is high, and operation cost is high.

The invention discloses a garbage incinerator smoke gas treatment system, and belongs to the technical field of smoke gas desulfurization environment protection. The garbage incinerator smoke gas treatment system comprises a temperature reducing tower, an absorption tower, a cloth bag dust remover and a chimney in sequential connection, wherein a water atomization spray head is arranged at the top of the temperature reducing tower; a smoke gas inlet is formed in the top of the temperature reducing tower; a smoke gas outlet is formed in the lower part of the temperature reducing tower; a secondary spraying device is arranged on the top of the absorption tower; a ripple water film absorbing device is arranged under the secondary spraying device; an active carbon spraying pipe and a powdery slaked lime spraying pipe are arranged on a flue for connecting the temperature reducing tower and the absorption tower; the absorption tower is connected with a quicklime slurry feeding pipe; the quicklime slurry feeding pipe is connected with a quicklime slurry proportioning system. After the garbage incineration smoke gas passes through the system, the smoke dust is reduced to about 30mg/m<3>; the HCl is reduced to about 40mg/m<3>; the SOX is reduced to about 150mg/m<3>.

The invention discloses a fuel nozzle, a solid fuel combustion system and a preheating combustion method. The nozzle comprises a straight cylinder part, and a cover is arranged above the straight cylinder part; a secondary air inlet is formed in the cover; the straight cylinder part comprises two cylinder sections with different diameters, the two cylinder sections with different diameters are fixedly connected, and the preheating fuel inlet and the tertiary air inlet are respectively formed in the two cylinder sections with different diameters. And the preheated fuel inlet is used for introducing preheated fuel. On the basis of preheating modification nitrogen reduction of the preheating combustor, re-gasification nitrogen reduction of a nozzle of the separation cavity, longitudinal on-way multi-layer tertiary air addition, airflow rotation of the separation cavity, on-way layered secondary gasification, nitrogen reduction and reaction retention time increase are achieved, the conversion rate of hot semicoke fuel is increased, and ultralow NOx emission and stable combustion are achieved.