Patents
Literature
Patsnap Copilot is an intelligent assistant for R&D personnel, combined with Patent DNA, to facilitate innovative research.
Patsnap Copilot

437results about How to "Reduce the difficulty of separation" patented technology

Method for preparing aromatic hydrocarbons and propylene simultaneously employing methanol/dimethyl ether

The invention discloses a method for preparing aromatic hydrocarbons and propylene simultaneously employing methanol / dimethyl ether, comprising the following steps: 1) placing raw materials containing methanol or / and dimethyl ether, metals and molecular sieve based catalyst which is modified through silanizing in a first fixed bed reactor to perform catalytic reaction; 2) separating the products obtained in step 1) to obtain propylene, then placing propylene in a second fixed bed reactor with molecular sieve based catalyst which is modified by using metals to react, then performing aromatization on the obtained product in step 1) and obtaining aromatic hydrocarbons; then separating to obtain toluene and sending toluene back to the outlet of the first fixed bed reactor as a raw material. In the method, methanol is converted and prepared to aromatic hydrocarbons while propylene is produced at the same time and the content of paraxylene in aromatic hydrocarbons is high. In the products prepared by the method, the content of propylene can reach above 20%, the content of aromatic hydrocarbons can reach above 58wt% and the content of paraxylene in aromatic hydrocarbons is more than 35wt%.
Owner:CHINA NAT OFFSHORE OIL CORP +2

Extraction and purification process for cordycepin in cordyceps militaris link

The invention provides an extraction and purification method of cordycepin from Cordyceps militaris, and belongs to the deep-processing technical field of agricultural products. The method comprises the following steps: crushing Cordyceps militaris raw material, mixing the raw material with water at 1:20 raw material/water ratio, performing ultrasonic extraction, and performing centrifugal filtration on obtained extracting solution and pouring in a macroporous resin column at the adsorption flow of 1.8BV/hr; taking 15% methanol aqueous solution as an eluant to perform resin column elution, and decompressing and condensing obtained eluent at the temperature of 60 DEG C by a rotary evaporator to obtain Cordyceps militaris cordycepin concentrate. The method can help realize aqueous solution extraction of the cordycepin from the Cordyceps militaris raw material at low temperature, and the extraction rate reaches 85%; and polysaccharide and protein can be removed from the extract by macroporous resin separation and purification, thus the content of the cordycepin in the extract can reach 10%. The cordycepin in the Cordyceps militaris product has high activity, can be taken as a raw material for producing cordycepin monomer and can also be directly taken as an additive of health products and functional food, thus the cordycepin has wide market development prospect.
Owner:JIANGSU ACADEMY OF AGRICULTURAL SCIENCES

Combined coal tar whole fraction hydroprocessing system and application thereof

The invention relates to a combined coal tar whole fraction hydroprocessing system and an application thereof. The system comprises a desalination dehydration impurity-removing refining system 1 which is connected with a hydrogen compressor 11 and an up-flow moving bed hydrofining reactor 3 respectively through one hydrogenation feeding pump 12, the up-flow moving bed hydrofining reactor 3 is respectively connected with a catalyzer on-line feeding system 2 and two series connection fixed bed hydrofining reactors 4, the fixed bed hydrofining reactors 4 are connected with separators 5, the separators 5 are respectively connected with a hydrogen refining system 10 and a flash tower 6, the flash tower 6 is connected with a fixed bed hydrocracking reactor 7 through the other hydrogenation feeding pump 12 and then sequentially connected with a fixed bed hydrofining reactor 8, the separators 5 and a fractionating tower 9. Compared with combined coal tar whole fraction hydroprocessing systems in the prior art, the combined coal tar whole fraction hydroprocessing system has the advantages that the process is simpler, the conversion rate is higher, operation is stable, product properties are good, and the system can be used for production processes of excellent light fuels by poor raw materials such as various coal tar, shale oil and residual oil.
Owner:袁继海 +2

Method for preparing aromatic hydrocarbons and propylene simultaneously employing methanol/dimethyl ether

The invention discloses a method for preparing aromatic hydrocarbons and propylene simultaneously employing methanol / dimethyl ether, comprising the following steps: 1) placing raw materials containing methanol or / and dimethyl ether, metals and molecular sieve based catalyst which is modified through silanizing in a first fixed bed reactor to perform catalytic reaction; 2) separating the products obtained in step 1) to obtain propylene, then placing propylene in a second fixed bed reactor with molecular sieve based catalyst which is modified by using metals to react, then performing aromatization on the obtained product in step 1) and obtaining aromatic hydrocarbons; then separating to obtain toluene and sending toluene back to the outlet of the first fixed bed reactor as a raw material. In the method, methanol is converted and prepared to aromatic hydrocarbons while propylene is produced at the same time and the content of paraxylene in aromatic hydrocarbons is high. In the products prepared by the method, the content of propylene can reach above 20%, the content of aromatic hydrocarbons can reach above 58wt% and the content of paraxylene in aromatic hydrocarbons is more than 35wt%.
Owner:CHINA NAT OFFSHORE OIL CORP +2

Method for preparing gentio-oligosaccharide by using immobilized beta-glucosidase

The invention discloses a method for preparing gentio-oligosaccharide by using immobilized beta-glucosidase. The method for preparing the gentio-oligosaccharide by using the immobilized beta-glucosidase comprises the following steps of: 1) preparing beta-glucosidase through solid-state fermentation of Aspergillus niger; 2) immobilizing the beta-glucosidase by a crosslinking-embedding method; and 3) producing the gentio-oligosaccharide by transforming glucose by using the immobilized beta-glucosidase. The recovery rate of enzyme activity of an immobilized enzyme prepared by the method is up to 60 percent, and the conversion rate of a substrate, namely the glucose converted by the immobilized enzyme is 45 percent; and the stability and pH tolerance of the immobilized enzyme are remarkably improved, the mechanical strength is high, the immobilized enzyme can be continuously and repeatedly used for 4 to 6 bathes, and the enzyme activity is kept unchanged. The utilization rate of the gentio-oligosaccharide produced by an enzyme method is improved, the production cost and difficulty in separation and purification of the gentio-oligosaccharide are reduced, and the method is suitable for large-scale continuous production and has a great significance for improving the technical level of the production of the gentio-oligosaccharide in China.
Owner:SHAANXI UNIV OF SCI & TECH

Technique for reclaiming vanadium and iron from high-vanadium high-iron steel slag

A novel technology is used for recycling iron and vanadium from calcium-rich or iron-rich steel slag. The invention relates to a metallurgical method of extracting vanadium, in particular to a method that extracts vanadium or iron from abandoned steel slag with multidisciplinary technologies. The technology has the following procedures: (1) The calcium-rich or iron-rich steel slag is crushed, the iron contained in the steel slag is recycled by magnetic separation, and the material that will correspondingly change low-valent vanadium is roasted into high-valent vanadium contained in the material, or the material is first roasted and then magnetic separated; (2) the material is soaked with 95-98 percentage concentrated sulfuric acid, and then solid-liquid separation is conducted; (3) the acidity of lixivium is adjusted, to make sure the pH of the lixivium is in 1.0 to 2.3, and the oxidation-reduction potential is -1000 to 200mv; (4) Extraction above grade two is adopted, the extraction phase ratio O/A is 1/6 to 1/1, and then the aqueous phase unloaded; (5) the organic washing is applied in the load to remove iron, and the washing agent used is sulphate; (6) 0.25M to 1.5M alkaline solution is adopted as a stripping agent for back-extraction, with a phase ratio of O/A 1/1 to 6/1, so as to deposit vanadium contained in solution. The invention is characterized by simple technology, low cost, small environmental pollution and high recovery ratio in the process of extracting vanadium and iron from calcium-rich or iron-rich steel slag.
Owner:KUNMING UNIV OF SCI & TECH

Method for adsorbing and separating paraxylene and ethylbenzene from C8 aromatic components

The invention discloses a method for adsorbing and separating paraxylene and ethylbenzene from C8 aromatic components. The method comprises the following steps: performing liquid-phase adsorption and separation on C8 aromatic hydrocarbons, thereby obtaining extracted oil rich in paraxylene and raffinate oil rich in ethylbenzene, m-xylene and o-xylene; introducing the raffinate oil into a gas phase adsorption and separation column, adsorbing ethylbenzene from the raffinate oil under the conditions of 190-270 DEG C, 0.4-0.8MPa and gas phase, allowing the non-adsorbed components to flow out of the gas phase adsorption and separation column to serve as adsorption residues, and purging an adsorbent bed layer by using purge gas under the pressure not less than the adsorption pressure, wherein the purged intermediate components is used as gas phase adsorption feedstock; reducing the pressure to 0.1-0.3 MPa, introducing the purge gas to desorb the adsorbed ethylbenzene so as to obtain the aspirate, performing xylene isomerization on the adsorption residues, wherein the isomerization products are taken as raw materials of the above liquid phase adsorption and separation. According to the method, the high-purity paraxylene and ethylbenzene can be separated from the C8 aromatic components, the adsorption residues hardly contain ethylbenzene, and isomerization can be performed under the non-hydrogen and low-temperature conditions.
Owner:CHINA PETROLEUM & CHEM CORP +1

Method for separating isoprene by combined rectification

The invention relates to a combined isoprene rectification and separation method, mainly aimed at solving the problems in prior art that when to separate and crack the diolefin in c_5 fraction, the raw materials have to enter a thermal dimerization reactor first, resulting in great losses of isoprene and cyclopentadienyl, and that because the boiling points of isoprene and cyclopentadienyl are nearly the same, the cyclopentadienyl affects the purity of the product isoprene and a part of cyclopentadienyl is lost, and particularly the problem that the isoprene knockout tower has high temperature and is energy-consuming. The invention makes the c_5 materials enter the isoprene knockout tower2 from the middle; after separation, material flow I containing isoprene comes out from the top of the tower and the material flow II containing cyclopentadienyl comes out from the bottom of the tower for later processing. Then the material flow I enters the cyclopentadienyl recycling tower from the middle part, after separation the material flow III coming out from the top of the cyclopentadienyl recycling tower enters the follow-up isoprene refining process and the cyclopentadienyl material flow coming out from the bottom of the cyclopentadienyl recycling tower circulates to the middle part of the isoprene knockout tower2. With such technique proposal, the invention solves the problems, thus the invention can be applied to the industrial production of separating the diolefin in c_5 fraction.
Owner:SINOPEC SHANGHAI ENG

Methyl methacrylate synthesis process

ActiveCN110981727AReduce cycle energy consumptionCracking the separation puzzleOrganic compound preparationCarboxylic acid esters preparationPropanoic acidHydrogenation reaction
The invention discloses a methyl methacrylate synthesis process comprising the steps: carrying out condensation reaction on the reaction raw materials, liquefying and separating out a mixture of methanol and methyl acetate, circulating, separating out a mixture of methanol and methyl acrylate, carrying out hydrogenation reaction to obtain a mixture of methanol and methyl propionate, carrying out areaction on the mixture with a formaldehyde source, liquefying a reaction product gas flow, separating out a mixture of methanol and methyl propionate to obtain a methanol-free MMA crude product liquid, separating the mixture of methanol and methyl propionate, and respectively circulating. According to the method, the mixture of methanol and methyl acetate, the mixture of methanol and methyl acrylate and the mixture of methanol and methyl propionate are gradually separated in an azeotropic manner, so that the energy consumption of methanol separation circulation is reduced; methanol and methyl acrylate azeotrope is used as a raw material to be fed into a hydrogenation reactor, so that the separation difficulty is reduced; formaldehyde is separated from the methanol-free MMA crude productliquid, and the difficulty of further refining is lower; the separation problem of a methanol-containing multi-component complex easily-polymerized system is effectively solved, and a powerful supportis provided for MMA synthesis of a methyl acetate route.
Owner:SOUTHWEST RES & DESIGN INST OF CHEM IND

Method and special device for heterogeneous catalyzed synthesis of triacetonamine

The invention belongs to the technical field of preparation of hindered amine light stabilizer midbody and pharmaceutical midbody triacetonamine, and particularly relates to a method and a special device for heterogeneous catalyzed synthesis of triacetonamine. The technical scheme is that a cone base reaction kettle consisting of a straight cylinder section and a cone cylinder section is applied, and a water knockout drum formed by a tubular type membrane tube is arranged in the cone base reaction kettle; heterogeneous catalyst and acetone are added in the reaction kettle; after stirring and heating, ammonia gas is filled for reaction; the procedures of separating water by the water knockout drum, cooling, stopping mixing, separating water and standing are carried out, and reaction fluid is discharged and filtered to obtain a crude product of triacetonamine; finally, the crude product is rectified to obtain the high-purity triacetonamine product. In the invention, the heterogeneous catalyst is applied to replace the homogeneous catalyst, thus the separating difficulty of the catalyst is reduced, the high saline-alkali waste water generated from separation process of homogeneous catalyst is avoided; the reaction water is separated from the reaction process, the yield of triacetonamine is improved, and the water separating cost of the rectifying technique is reduced. The content of organic matters in separated water of the water knockout drum is low, and water disposal cost is reduced.
Owner:HENGSHUI KAIYA CHEM

Catalyst system for preparing hydrocarbons and use thereof

The invention discloses a process for producing of aromatic hydrocarbons and co-production of light hydrocarbons through synthesis gas conversion and a catalyst used in the process; a catalyst systemhas synthesis gas conversion activity and aromatic hydrocarbon /light hydrocarbon synthesis activity. The synthesis gas conversion activity is provided by a metal oxide catalyst, the aromatic hydrocarbon /light hydrocarbon synthesis activity is provided by a solid acid catalyst including a ZSM-5 or ZSM-11 molecular sieve and modified molecular sieve. The active component of the metal oxide is preferably selected from one or at least one of Cr, Zr, Mn, Ce, La, Ti, In and Zn. The silicon-aluminum ratio of the ZSM-5 or ZSM-11 molecular sieve / the modified molecular sieve ranges from 12-250. Thecatalyst form comprises a composite catalyst or a multi-section catalyst system. Under the conditions that the molar ratio of H2 to CO in the raw material is 0.25-5.0, and/or the reaction temperatureis 300-500 DEG c and/or the pressure is 0.5-10.0 MPa, and/or the volume space velocity is 1000-20000 h<-1>, the synthesis gas can be efficiently converted in one-section or multi-section catalyst systems to generate aromatic hydrocarbon and light hydrocarbon products. The process is a non-fischer-tropsch route, and is a novel route for producing of the aromatic hydrocarbons and co-production of the light hydrocarbons through synthesis gas conversion by virtue of a one-step method.
Owner:CHINA PETROLEUM & CHEM CORP +1

Technical method for preparing aromatic hydrocarbon through methanol aromatization

The invention relates to a technical method for preparing aromatic hydrocarbon through methanol aromatization. The technical method is characterized by comprising the steps: firstly, reacting methanol in a fixed-bed reactor filled with a methanol hydrocarbonylation reaction catalyst and an olefin aromatization catalyst, enabling the reacted product to enter a reactor filled with a non-aromatic cracking agent, reacting, separating the product to obtain dry gas, C<3+> non-aromatic hydrocarbon and aromatic hydrocarbon, wherein the dry gas and the aromatic hydrocarbon are output from the system as products, the C<3+> non-aromatic hydrocarbon is dehydrogenated after entering a dehydrogenation reactor, the dehydrogenated C<3+> non-aromatic hydrocarbon returns a methanol hydrocarbonylation reactor for continuing reaction. Through the technique, the methanol conversion, olefin aromatization, non-aromatic cracking and alkane dehydrogenation technology are combined, so that no only can the yield and selectivity of aromatic hydrocarbon be improved, but also the separation difficulty of aromatic hydrocarbon can be lowered. Through the technique, the total yield of the aromatic hydrocarbon (based on mass of methanol) can achieve 30-34%.
Owner:CHINA NAT OFFSHORE OIL CORP +2

Matched plastic film residue separation device for cotton picker

The invention relates to a matched plastic film residue separation device for a cotton picker. The matched plastic film residue separation device comprises a separation chamber. A large net-shaped roller, a small net-shaped roller and an air-lock valve area arranged in the separation chamber. A cotton flow inlet, a plastic film residue outlet and a seed cotton outlet are arranged on the separation chamber. The large net-shaped roller and the small net-shaped roller are both of internal hollow structures, gauzes are arranged at the peripheries of outer layers of the net-shaped rollers, and the small net-shaped roller is arranged obliquely above the large net-shaped roller and close to the plastic film residue outlet. When the matched plastic film residue separation device works, the large net-shaped roller and the small net-shaped roller rotate in a counterclockwise mode. The air-lock valve structurally and mainly comprises a casing, an air-lock valve rotating shaft and a fan blade arranged on the air-lock valve rotating shaft. In an initial stage for picking cotton, sundries in seed cotton can be removed, so that a serial of related work procedure links of opening, removing residues and the like can be eliminated after seed cotton is harvested, and energy consumption is reduced. The device can greatly reduce sundry separation difficulty and is simple in structure, economical and practical.
Owner:SHIHEZI UNIVERSITY
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products