146results about "Crystallisation purification/separation" patented technology

The invention provides a method for synthesizing 1, 2-bis (4-vinyl phenyl) ethane, which comprises the following steps: adding a first solvent, methyl triphenyl phosphine halide and strong alkali into a reaction flask, and uniformly stirring to obtain a first mixed solution; heating the first mixed solution and carrying out reflux reaction for 1 hour; dropwise adding a 1, 2-bis (p-formaldehyde phenyl) ethane solution until the reflux reaction is finished to obtain a second mixed solution; reducing the temperature of the second mixed solution to room temperature, and adjusting the pH value of the second mixed solution to obtain a first solution; layering the first solution, and taking an organic layer; adding a polymerization inhibitor into the organic layer to obtain a second solution; concentrating the second solution to obtain a 1, 2-bis (4-vinyl phenyl) ethane crude product; adding a poor solvent into the crude product, stirring and crystallizing; filtering the crystal to obtain a filter cake, adding a second solvent into the filter cake, and washing and drying the filter cake to obtain 1, 2-bis (4-vinyl phenyl) ethane; the method for synthesizing the BVPE is simple and low in raw material cost, and the synthesized BVPE is high in purity and free of product isomeride.

The invention relates to the technical field of organic photoelectric materials, in particular to a co-assembly method for improving energy transfer efficiency of chromophores, a co-assembly body and application. The specific method comprises the following steps: co-assembling a donor substance and perfluorinated aromatic hydrocarbon in a solvent system to prepare a donor-perfluorinated aromatic hydrocarbon compound; the method comprises the following steps: co-assembling an acceptor substance and perfluorinated aromatic hydrocarbon in a solvent system to prepare an acceptor-perfluorinated aromatic hydrocarbon compound; the preparation method comprises the following steps: co-assembling a donor-perfluorinated aromatic hydrocarbon compound and an acceptor-perfluorinated aromatic hydrocarbon compound in a solvent system to prepare a crystal-induced energy transfer precise co-assembly body; the donor substance is 9, 10-bis (phenylethynyl) anthracene, and the perfluorinated aromatic hydrocarbon is octafluoronaphthalene; the acceptor substance is 5, 12-bis (phenylethynyl) tetracene. The problems of high energy dissipation and low FRET efficiency of the donor-acceptor pair with weak aggregation emission in the fluorescence resonance energy transfer process are solved.

The present invention relates to a method for synthesizing small-sized organic nanocrystals using cadmium telluride quantum dots, and belongs to the field of nano synthesis technology. The method uses functionalized quantum dots as seeds to synthesize organic molecular crystals through a seed growth method, and the synthesized organic nanocrystals have uniform sizes, and the sizes are all around 30nm. The method is simple and universal, and provides a new path for accurately controlling the size of organic molecular crystals.

[Problem] To provide a method capable of producing a monocyclic aromatic hydrocarbon such as benzene or xylene effective as a base raw material, with a naphtha raw material containing renewable naphtha. [Solution] A method for producing at least one monocyclic aromatic hydrocarbon of benzene or xylene with a naphtha raw material containing renewable naphtha, the method including step (A-1) of pyrolyzing the naphtha raw material in the presence of water vapor, to produce and separate toluene, and step (A-2) of subjecting toluene to disproportionation reaction or transalkylation reaction, to produce and separate at least one monocyclic aromatic hydrocarbon of benzene or xylene.

The invention relates to the technical field of chemical separation and purification, and discloses a method for separation and purification of taxadiene from tobacco and GC-MSMS quantitative detection.The method for separation and purification of taxadiene from tobacco comprises the following steps that S1, tobacco leaves are made into powder, an extracting agent is added, ultrasonic extraction is conducted for multiple times, and extract liquor is obtained; s2, evaporating the extract to dryness, adding an organic solvent, and dissolving to form a concentrated solution; s3, the concentrated solution is added into a silica gel column for gradient elution, and an extraction sample is obtained; and S4, evaporating the extracted sample to dryness, adding acetonitrile for dissolving, and carrying out secondary recrystallization to obtain purified taxadiene. According to the method, the efficiency and purity of separating the taxadiene from the tobacco are improved, and the taxadiene is accurately quantified.

The invention provides a p-xylene crystallization tower. The p-xylene crystallization tower comprises a tower body, a cooling structure and a scraper structure, mixed xylene is contained in the tower body; the cooling structure comprises a sealing plate and liquid conveying pipes arranged at the upper end and the lower end of the sealing plate respectively, and the sealing plate surrounds the periphery of the tower body; the sealing plate is wavy; the sealing plate comprises a plurality of wave trough parts and a plurality of wave crest parts which are alternately arranged, the wave trough parts are tightly connected with the periphery of the tower body, and the sealing plate and the periphery of the tower body define a circulation channel extending in the vertical direction between any two adjacent wave trough parts; the liquid conveying pipes are arranged on the periphery of the tower body in a surrounding mode, and the two liquid conveying pipes communicate with the multiple circulation channels correspondingly. And the refrigerating medium is input into the circulation channel through the liquid conveying pipe. And the mixed xylene is cooled under the action of the refrigerating medium, and paraxylene is crystallized and separated out on the inner circumferential wall of the tower body. And the scraper structure scrapes crystals on the tower body. According to the p-xylene crystallization tower, a refrigerating medium is in close contact with the tower body, so that the dissipation of cold energy is effectively reduced, and the refrigerating effect is improved.

The invention discloses a method for synthesizing 1, 2-bis (4-vinylphenyl) ethane, which comprises the following steps: S1, under the protection of nitrogen, taking 4-vinylbenzyl chloride as a solvent and a reactant, and reacting in the presence of iodine, magnesium metal and ethylene glycol diethyl ether to generate the 1, 2-bis (4-vinylphenyl) ethane; s2, after the reaction is finished, heating, and filtering to remove magnesium chloride while the solution is hot; and S3, cooling and crystallizing to separate out the product 1, 2-bis (4-vinyl phenyl) ethane, and filtering and separating the product to obtain mother liquor which can be directly used for synthesizing the 1, 2-bis (4-vinyl phenyl) ethane. The method has the beneficial effects that the solubility of the product 1, 2-bis (4-vinylphenyl) ethane in 4-vinylbenzyl chloride can be effectively adjusted by introducing the additive ethylene glycol diethyl ether (EGDE), magnesium chloride can be removed by directly heating and filtering while the solution is hot after the reaction, then the product can be obtained by cooling and crystallizing the mother liquor, the process of the method is shorter than that of the existing method, a washing step is omitted, and the method is suitable for industrial production. And subsequent magnesium sulfate mother liquor drying and harsh solvent dehydration steps are avoided.

This invention discloses a method for controlling photon spin-orbit coupling in an organic alloy microcavity, belonging to the field of optical microcavity technology. This invention prepares β-type Pe by doping different amounts of DCA into Pe using a volatilization method. 1‑x DCA x An organic alloy, wherein x ≤ 20 wt%, allows for the controllability of crystal color from yellow-green to orange-red. Furthermore, this organic alloy exhibits birefringence, and its application in the fabrication of optical microcavities allows for the observation of TE-TM spin-orbit coupling and Rashba-Dresselhaus spin-orbit coupling within the microcavities. This provides a novel type of microcavity for studying the interaction between light and matter in organic alloy microcavities, and the controllability of photon spin-orbit coupling within these microcavities can be achieved by adjusting the value of x.

The present invention relates to the technical field of polycyclic aromatic hydrocarbon separation, and provides a polycyclic aromatic hydrocarbon separation method. In the present invention, firstly, a mixed solvent and a mixture to be separated are mixed and then filtered to obtain a filter cake and a filtrate, then a back-extractant and the filtrate are mixed and then separated, wherein the mixed solvent is a naphthyl mixed solvent or an imidazole mixed solvent, and the mixture to be separated is a mixture containing a bicyclic aromatic hydrocarbon and a tricyclic aromatic hydrocarbon or a mixture containing a tricyclic aromatic hydrocarbon and a tetracyclic aromatic hydrocarbon. According to the present invention, the mixture containing the bicyclic aromatic hydrocarbon and the tricyclic aromatic hydrocarbon is separated by using the naphthyl mixed solvent, the mixture containing the tricyclic aromatic hydrocarbon and the tetracyclic aromatic hydrocarbon is separated by using the imidazole mixed solvent, and the naphthyl mixed solvent or the imidazole mixed solvent can be recycled. Additionally, the separation method provided by the present invention has simple steps, low energy consumption and a simple technological process.

The invention relates to the technical field of alkyl anthracene production, and discloses a separation method of an anthracene alkylation reaction product, which comprises the following steps: pretreating the anthracene alkylation reaction product to remove part of anthracene; mixing the pretreated product with an entrainer, and rectifying at the temperature of 100-250 DEG C and the pressure of 1-120 kPa to obtain a light component I and a heavy component I; the light component I contains an azeotrope of a reaction solvent and an entrainer in the anthracene alkylation reaction product; the heavy component I is rectified at the temperature of 100-300 DEG C and the pressure of 0.5-100 kPa, and a light component II and a heavy component II are obtained; the light component II contains an azeotrope of anthracene and an entrainer; and carrying out cooling crystallization on the heavy component II, and carrying out solid-liquid separation to obtain alkyl anthracene. By adopting the separation method provided by the invention, the system can stably operate for a long time, and meanwhile, higher yield and purity of anthracene and alkyl anthracene can be realized.

The crystallization purification preparation system for 2, 6-dimethylnaphthalene comprises a suspension stirring crystallizer and a crystal filter, the suspension stirring crystallizer is connected to one end of the crystal filter, and the other end of the crystal filter is connected with a residual liquid tank and a static crystallizer; a mother liquid tank and a finished product tank are arranged on the first pipeline between the static crystallizer and the crystal filter; meanwhile, the residual liquid tank, the mother liquid tank and the static crystallizer are also respectively connected with a waste removal and discharge pipeline; wherein the suspension stirring crystallizer is connected with a cooling and heating all-in-one machine through a cooling and heating medium pipeline, and the static crystallizer is also connected with the cooling and heating all-in-one machine through the cooling and heating medium pipeline. According to the method, high-purity 2, 6-dimethylnaphthalene is obtained from low-value petrochemical raw materials by adopting a crystallization purification method.

The invention discloses a two-dimensional organic transverse heterogeneous crystal and a preparation method and application thereof.According to the preparation method, a step-by-step micro-spacing air sublimation method is adopted, the growth temperature of a secondary crystal is precisely regulated, effective control over the molecular diffusion and deposition process is achieved, and the yield of the two-dimensional organic transverse heterogeneous crystal is improved. And the two-dimensional organic transverse heterogeneous crystal with the adjustable epitaxial layer thickness can be simply and conveniently prepared. According to the invention, unique optical characteristics of the two single-component crystals are fully utilized, and optical signal emission of different wavebands can be realized at different polarization angles. By means of the characteristic, the wide application potential is achieved in the fields of optical sensing, optical communication and the like, and the requirement for diversity of optical signal wavebands can be met.

The utility model relates to recovery device technical field, concretely is a kind of benzene recovery device, including waste oil buffer tank, waste oil buffer tank is connected with the top of crude benzene crystallization tank by pipeline, the bottom of crude benzene crystallization tank is connected with the top of fine benzene rectifying column by pipeline one, and cooling pipe is wound in side portion, and cooling pipe is connected with freezer;Pipeline one is provided with feed pump;The top of fine benzene rectifying column is connected with fine benzene condenser by pipeline, and bottom is connected with heavy residue discharge pipe;Fine benzene condenser is connected with fine benzene buffer tank by pipeline two;The utility model is through being provided with crude benzene crystallization tank and fine benzene rectifying column, first crystallization comes out crude benzene, and then distills crude benzene, and the fine benzene of distillation comes out, to realize the extraction and recovery of benzene, avoid the waste of resources, reduce cost.

The application provides a method for preparing beta-methylnaphthalene from a methylnaphthalene-containing fraction based on solution homogenization crystallization separation, and comprises the following steps: pumping the methylnaphthalene-containing fraction into a fluidized bed reactor, performing primary cooling treatment, and performing ultrasonic treatment through an ultrasonic device arranged on the inner wall of the fluidized bed reactor, and then filtering after the crystallization treatment; re-heating the solid in the fluidized bed reactor, then performing secondary cooling treatment and ultrasonic treatment at the same time, and then filtering after the crystallization treatment; re-heating the solid in the fluidized bed reactor, then performing third cooling treatment, and performing ultrasonic treatment at the same time, and then filtering after the crystallization treatment, collecting the filter residue, and then drying to obtain high-purity beta-methylnaphthalene. The method combines the fluidized bed reactor with the ultrasonic treatment technology, and adopts step-by-step crystallization, so that impurities are effectively removed, high-purity beta-methylnaphthalene is obtained, and the yield of the product is obviously improved.

Disclosed are apparatuses and processes for preparation and conversion comprising / using: a fractionation chain (4-6) that produces a xylene fraction (24); a xylene separation unit (10) that treats the xylene fraction to produce a para-xylene extract (39) and a raffinate (40); an isomerization unit (11) treating the raffinate to produce an isomerization product (42) of xylenes fed to the fractionation chain; the synthesis gas production unit (14; 15) that treats the hydrocarbon feedstock (30) to produce a synthesis gas (34) containing CO and CO2; a methanol synthesis reaction section (50) that treats the synthesis gas (34) to produce methanol (51); a toluene alkylation reaction section (13) treating the toluene-containing fraction (23) with methanol (51) to produce an alkylation effluent (32) containing xylene and fed to the fractionation chain.

The invention belongs to the technical field of photothermal conversion materials, and discloses a preparation method and application of an inorganic-organic hybrid polyoxotungstate photothermal material with wide spectrum absorption. The structural formula of the photo-thermal material is Per4W10O32, the crystal structure belongs to a triclinic system, the space group is P-1, and the photo-thermal material has specific unit cell parameters. The preparation method comprises the following steps: oxidizing perylene molecules through constant current electrolysis in a mixed solvent system containing perylene molecules and a decatungstate precursor in an electrochemical oxidation manner, and assembling the oxidized perylene molecules with decatungstate anions to form bulk crystals; the photo-thermal material has continuous strong absorption in a region from ultraviolet light to short wave infrared, the photo-thermal conversion efficiency is as high as 98.24%, when the photo-thermal material is applied to the fields of solar driven interface photo-thermal evaporation and water treatment, the evaporation rate of a two-dimensional system is 1.89 kg.m <-2 >. H <-1 >, the evaporation rate of a three-dimensional hydrogel system is increased to 3.02 kg.m <-2 >. H <-1 >, salt deposition can be inhibited in long-term seawater desalination operation, and the photo-thermal material has a good application prospect. Fresh water quality meets drinking water standards.

The present application relates to the field of basic organic chemistry synthesis, and particularly to a high-yield preparation method of o-terphenyl based on hydrogen participation; comprising the steps of preparing a catalyst mixed solution, preparing a reaction mixed solution, filling micro-pressure hydrogen, heating and hydrogenation coupling reaction, rough extraction through reduced pressure distillation, and recrystallization and drying; a pre-assembly reaction precursor is formed by a bidentate phosphine bidentate phosphine ligand and a supported palladium catalyst, and a coupling reaction occurs with diphenyl under the cooperation of micro-pressure hydrogen and an acidic cocatalyst; the present application does not need to use traditional halogenated aromatic hydrocarbons and organic metal reagents, solves the problems of isomer mixing and difficult separation and halogen residue affecting the performance of downstream optoelectronic materials, realizes the preparation of o-terphenyl, and simplifies the separation and purification process.

The invention provides a multi-stage washing production process of high-concentration p-xylene, which comprises the following steps: cooling and crystallizing a raw material under a first temperature condition to obtain first crystal mush; carrying out solid-liquid separation on the first crystal mush, washing raw materials and part of products to obtain first crystals, first filtered mother liquor and first eluate, and melting the first crystals to obtain a first p-xylene product; sending part of the first filtered mother liquor to a second temperature condition for cooling crystallization to obtain second crystal mush; repeating the steps on the second crystal mush to obtain a second p-xylene product; and cooling and crystallizing part of the second filtered mother liquor under a third temperature condition to obtain third crystal mush, and repeating the steps on the third crystal mush to obtain a third p-xylene product. The problems that the crystal transfer amount is large and difficult and the crystal particle circulation amount is large during p-xylene production can be solved.

This invention provides a method for purifying mesitylene through suspension melt crystallization, belonging to the field of fine chemical separation technology. By adding a crystallization aid to assist in the suspension melt crystallization of mesitylene, this invention overcomes the limitations of traditional crystallization separation. The addition of the crystallization aid interacts with impurities in the crude product, effectively altering the crystallization behavior of the impurities and inhibiting their entry into the mesitylene lattice during crystal growth. This reduces the amount of impurities trapped during mesitylene crystallization, accelerates the crystallization process, and reduces the number of multi-stage crystallization. Without altering the main molecular configuration of mesitylene, this invention achieves highly efficient separation and purification of mesitylene, significantly improving its purity and yield. It solves the problem of isomer separation and overcomes the technical bottleneck of low efficiency in the existing mesitylene purification and separation process.

The utility model relates to the technical field of naphthalene water separation, in particular to industrial naphthalene water separation and recovery equipment which comprises a condensation kettle and a bottom plate, a collecting barrel is placed at the upper end of the bottom plate, a discharging valve pipe is connected to the lower side of the condensation kettle in a penetrating mode, an inner threaded cover is fixedly connected to the outer wall of the discharging valve pipe, and a threaded ring is connected to the inner wall of the inner threaded cover in a threaded mode. The lower end of the threaded ring is fixedly connected with a collecting net barrel, and a bearing barrel is arranged on the outer side of the collecting net barrel. The solid naphthalene and the water in the condensation kettle enter the collecting net barrel, the solid naphthalene can be further isolated in the collecting net barrel, and the water falls into the receiving barrel through the meshes and flows into the collecting barrel, so that the solid naphthalene and the water can be collected through the collecting net barrel and the collecting barrel respectively, and after collection is completed, the solid naphthalene and the water are separated from each other. And the receiving barrel and the collecting net barrel can be taken down in opposite steps, so that the solid naphthalene and the water can be conveniently separated and recycled during discharging, and the purpose of improving the operation simplicity is further achieved.

The application provides a crystallization method of refined fluorene, which comprises the following steps: adding a raw material fluorene fraction into a mixed solution, carrying out a first beating and washing at normal temperature, and obtaining crude fluorene through centrifugal separation; mixing the crude fluorene with a solvent A, stirring and heating to 65-85 DEG C, cooling to 5-30 DEG C after the solid part is dissolved, keeping the temperature for 1 h, and obtaining industrial fluorene through centrifugal separation, and the mother liquor is used as a washing agent to participate in the first beating and washing. The method has simple and easy-to-control operation conditions and low cost. Through reducing the high-temperature operation time, using a high-boiling and low-volatility solvent to reduce the solvent loss in the crystallization process, using a single solvent to facilitate solvent recovery, using the mother liquor in the process to increase the yield and reduce the solvent consumption, using the beating and washing mode in the first step operation to operate at normal temperature, reducing the energy consumption and shortening the process cycle, and cooling and crystallizing in the second step operation, the crystal part is dissolved, the remaining solid is used as a crystal seed, so that the crystallization process is controllable, the primary burst nucleation is avoided, and the walling condition is reduced.

A method for producing para-xylene (PX) includes introducing a C8 aromatic-containing composition to a xylene rerun column to separate the C8 aromatic-containing composition into a xylene-containing effluent and a heavy effluent and passing the xylene-containing effluent to a PX processing loop that includes a PX recovery unit operable to separate PX from the xylene-containing effluent, a membrane isomerization unit operable to convert a portion of the MX, OX, or both to PX, an EB dealkylation unit operable to dealkylate EB to produce benzene, toluene, and other C7- compounds, and a membrane separation unit operable to produce a permeate that is PX-rich and a retentate that is PX-lean. The permeate is passed to the PX recovery unit for recovery of PX, which the retentate is bypassed around the PX recovery unit circulated through the xylene processing loop.

The present application relates to a kind of device and method for extracting high-purity chemicals from coal tar wash oil fraction, comprising: naphthalene separation column, methylnaphthalene separation unit, acenaphthene-fluorene-dibenzofuran separation unit;Methylnaphthalene separation unit includes methylnaphthalene separation tower, β-methylnaphthalene subunit and α-methylnaphthalene subunit connected in sequence;Acenaphthene-fluorene-dibenzofuran separation unit includes light removal tower, acenaphthene subunit, dibenzofuran subunit and fluorene subunit connected in sequence;The material outlet of the bottom of naphthalene separation column is connected with methylnaphthalene separation tower;The material outlet of the bottom of methylnaphthalene separation tower is connected with the material inlet of light removal tower.The device provided by the present application can effectively extract target chemicals in coal tar wash oil fraction by reasonable configuration of the device and coupling cooperation between devices, and obtain high-purity products.Compared with existing wash oil extraction chemical technology, it has higher efficiency, wider applicability and better product quality.

The invention relates to the technical field of production of 2, 6-dimethylnaphthalene, and discloses a production method and a production system of 2, 6-dimethylnaphthalene, and the production method comprises the following steps: (1) under a liquid phase condition, in the presence of an alkyl transfer catalyst, contacting reaction raw materials with a transfer alkylating agent to obtain a product mixture; the content of the 2, 6-dimethylnaphthalene is not less than 15wt% on the basis of the total content of the bicyclic aromatic hydrocarbon in the product mixture; (2) rectifying the product mixture to obtain a light component and a heavy component containing the dimethylnaphthalene isomer, and returning the light component to the step (1) to provide at least part of reaction raw materials; (3) mixing the heavy component obtained by rectification with a complexing agent, carrying out complexing crystallization, and then carrying out alkali washing to obtain a 2, 6-dimethylnaphthalene crude product; and (4) mixing the 2, 6-dimethylnaphthalene crude product with a solvent, and recrystallizing. The method has the advantages of high purity and high yield of the 2, 6-dimethylnaphthalene.

The application belongs to the field of photodynamic therapy, and specifically discloses a vitamin K co-crystal material for photodynamic therapy and a preparation method thereof. The vitamin K co-crystal material takes vitamin K as an electron acceptor, and the two carbonyl groups at the para positions of the vitamin K quinoid six-membered ring make the vitamin K exhibit electron deficiency, form an organic charge transfer complex with the electron acceptor, and self-assemble to form a co-crystal, so that the absorption spectrum of the system is widened, a wider wave band of light is more effectively utilized, the photodynamic therapy response wavelength of the vitamin K is adjusted from the ultraviolet region to the visible region and the near infrared region, the problem of low penetration depth and light damage caused by photodynamic therapy using light in the ultraviolet region is avoided, and the vitamin K has excellent photodynamic performance and good application prospects in surface sterilization and disinfection, treatment of body surface infection, and directional cancer treatment based on visible light or near infrared light.

The utility model discloses a p-xylene crystallization device which at least comprises a raw material input pipeline, the at least one crystallization unit is connected with the raw material input pipeline; the at least one separation unit is connected with the outlet of the crystallization unit; the mother liquor buffer tank is connected with an outlet of the separation unit; an inlet of the mother liquor pump is connected with an outlet of the mother liquor buffer tank; the subcooler is connected with an outlet of the mother liquor pump; the industrial wind input pipeline is connected with the other inlet of the mother liquor pump; and the industrial wind output pipeline is connected with the other outlet of the mother liquor pump. According to the p-xylene crystallization device provided by the utility model, the operation stability of the crystallization device can be improved.

The present invention discloses a production process and system for 2,3-dimethyl-2,3-diphenylbutane, including a reaction kettle, a crystallization kettle, a recovery kettle and a filtering and drying mechanism. The filtering and drying mechanism includes an annular water collecting tank, a rotary drive box and an annular drying tray. The output end of the rotary drive box is connected with a rotating support rod, the rotating support rod penetrates through the annular drying tray, and the top end of the rotating support rod is fixed with a first rotary joint. The top end of the first rotary joint is rotatably connected with a liquid inlet conduit, and a plurality of filtering barrels are connected around the first rotary joint. In the present invention, the raw materials are reacted in the reaction kettle and then fed into the crystallization kettle for crystallization. Then, the near-solution is fed into the filtering barrels through the liquid inlet conduit. The liquid in the filtering barrels is thrown out by the action of centrifugal force, and the solid crystals are filtered out and remain in the filtering barrels. Then, the wet crystals are poured into the annular drying tray and dried by blowing hot air, thereby completing the drying of the crystals. The integration degree is higher, and the production efficiency can be effectively improved.

The invention discloses a benzo C phenanthrene eutectic material and an application thereof. The benzo C phenanthrene eutectic material is a benzo C phenanthrene-F4TCNQ eutectic. When the benzo-C phenanthrene eutectic material is used as a photo-thermal imaging and treatment reagent, a photo-thermal phenomenon can be generated under the excitation of infrared light, the benzo-C phenanthrene eutectic material has obvious response to lasers with different powers, the heating rate is high, the heating rate is relatively high, and in addition, an area with relatively high temperature can be visualized through a photo-thermal effect. The co-crystal material can be excited in an infrared band, has obvious response to a magnetic field, is favorable for developing a more effective magnetic response type photo-thermal treatment reagent, can be excited in the infrared band, is favorable for deep imaging of tumor tissues, and can provide a new thought and method for research in the photo-thermal and magnetic diagnosis and treatment fields.

This invention belongs to the technical field of anthracene oil processing and production, and discloses a production method for increasing the anthracene and carbide content in crude anthracene products using crystal nucleus seeds. The method mainly involves cooling the heated raw anthracene oil to 75°C, then adding high-quality crystal nucleus seeds (70% anthracene content, 17% carbide content, and ≤1% mechanical impurities) to a crystallization tank at a mass ratio of 1:75. At this point, the high-quality crystal nucleus seeds promote the formation of new crystal nuclei in the anthracene oil liquid. As the temperature decreases, the newly formed crystal nuclei gradually grow. Simultaneously, the temperature is naturally lowered to below 65°C through stirring, and the cooling system in the crystallization tank is activated to further cool the temperature to 35-40°C. The mixture is then repeatedly fed and dried in a centrifuge to produce high-quality crude anthracene. This invention utilizes unique high-quality crystal nucleus seeds to achieve an anthracene content of over 40% and a carbide content of over 14% in crude anthracene even when the anthracene and carbide content in the raw anthracene oil is low or unstable, resulting in a superior-grade crude anthracene product.

The present disclosure provides systems and methods for producing aromatic compounds in high yield from mixed aromatic feed streams. Also disclosed are systems and methods for producing aromatic compounds in high yield from oxygenated hydrocarbons, such as carbohydrates, sugars, sugar alcohols, sugar degradation products, and the like.