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156results about How to "High aroma" patented technology

Method for extracting heavy liquefaction oil and intermediate-phase bitumen matter from coal liquefaction residuals and application thereof

The invention provides a method for extracting heavy liquefaction oil and an intermediate-phase bitumen matter from coal liquefaction residuals and application thereof. The method comprises the following steps of: adding coal liquefaction residual powder and an extraction solvent to a stirring kettle together for extraction to obtain extraction liquid and extraction residues; carrying out solid-liquid separation on the obtained extraction liquid and extraction residues; carrying out steam stripping on the obtained extraction residues, and recovering an organic phase after oil-water separation; mixing the extraction liquid with the organic phase, and then delivering into a solvent recovery unit; recovering the extraction solvent for recycling use or being returned to a liquefaction productprocessing unit by using a distillation method and/or an evaporation method, wherein residuals obtained after the extraction solvent is recovered are liquefaction residual extractives; delivering theobtained liquefaction residual extractives into a heat treatment unit, and separating the heavy liquefaction oil from the intermediate-phase bitumen matter by using a heating dry distillation method;and adding the obtained heavy liquefaction oil and other recycling solvents in a direct liquefaction process to a coal liquefaction solvent hydrogenation unit together.
Owner:CHNA ENERGY INVESTMENT CORP LTD +2

Extraction method of direct coal liquefaction residues and application of extracts

The invention relates to an extraction method of direct coal liquefaction residues and application of extracts. The extraction method comprises the following steps: a) adding coal liquefaction residue powder and a first extraction solvent to a stirred tank to undergo primary extraction; b) carrying out solid-liquid separation on the extracted mixture obtained in the step a) and recovering the first extraction solvent from the obtained liquid in a solvent recovery unit and recycling the first extraction solvent; c) obtaining extracts after recovering the first solvent and mixing the extracts with a second extraction solvent to undergo secondary extraction; d) carrying out solid-liquid separation on the extracted mixture obtained in the step c), obtaining heavy liquefied oil after recovering the second extraction solvent from the obtained liquid in the solvent recovery unit and then carrying out moderate hydrogenation on the heavy liquefied oil and other recycled solvents in a coal liquefaction solvent hydrogenation unit and using the product as the recycled solvent in the coal liquefaction process; and e) carrying out heat treatment on the asphaltic substances obtained in the step d) by heating and carbonizing to obtain mesophase asphalt and oils.
Owner:CHNA ENERGY INVESTMENT CORP LTD +2

Improved integrated process for hydrogenation and catalytic cracking of hydrocarbon oil

Disclosed is a combination process for improved hydrotreating and catalytic cracking of hydrocarbon oils, including: contacting residual oil, catalytic cracking cycle oil, and optional distillate oil with a hydrotreating catalyst under hydrotreating conditions in the presence of hydrogen followed by separation of the reaction products to obtain gas, hydrogenated naphtha, hydrogenated diesel oil, and hydrogenated tail oil; contacting the hydrogenated tail oil and optional normal catalytic cracking feedstock oil with a cracking catalyst under catalytic cracking conditions followed by separation of the reaction products to obtain dry gas, hydrogenated naphtha, liquefied petroleum gas, catalytic cracked gasoline, catalytic cracked diesel oil, and catalytic cracking cycle oil; wherein the hydrogenated tail oil and / or normal catalytic cracking feedstock oil are separated into at least two fractions, the light and the heavy fractions or normal catalytic cracking heavy feedstock oil and normal catalytic cracking light feedstock oil, prior to contacting the hydrogenated tail oil and / or normal catalytic cracking feedstock oil with the cracking catalyst. The process according to the present invention is especially suitable for conversion of hydrocarbon oils to produce more products of gasoline or diesel oil.
Owner:CHINA PETROCHEMICAL CORP +1

Simple process method of chestnut-flavor-type roasted green tea

The invention belongs to the field of tea leaf processing and particularly relates to a simple process method of chestnut-flavor-type roasted green tea. The method employs fresh leaves of six tea varieties including Long Jing 43, Wuniu early tea, Mei Zhan, Fuding Dahao and Fuyun 6. The method includes the steps of: picking fresh leaves, withering the leaves, performing de-enzyme, rolling the tea leaves, dry-frying the tea leaves in a cylinder, spreading the tea leaves, dry-frying the tea leaves in the cylinder again, spreading the tea leaves again, completely drying the tea, performing moisture regaining, performing fragrance enhancing to the tea leaves in a cylinder, and packaging the tea. The tea processing devices in the method are simple and are easy to operate. The method is low in cost. The chestnut-flavor-type roasted green tea has the following characters: dry tea is fine, tight and slightly-twisted, has a grey-green color with white fur, and has a significant chestnut flavor by smelling the tea while dry; when being brewed, the tea has a yellow and green color and is clear, has a strong fragrance and significant chestnut flavor and is refreshing and has a slight sweet taste; the tea is refreshing and has an sweet after taste. The tea residue has a deep-green and bright color and is uniform. The tea has durable taste when being brewed. The tea has excellent comprehensive quality and excellent economic beneifit.
Owner:福建省香入林茶业有限公司

Processing method capable of improving quality of Hunan medium/small leaf Congou black tea

The invention relates to a processing method capable of improving the quality of Hunan medium/small leaf Congou black tea. The processing method comprises the following steps: by adopting one of Yuntai Mountain tea, camellia sinensis, Zhuyeqi, Fuding large vellus, Baihaozao, Fuyun No.6, Bixiangzao, Xiangfucui, Mingfeng and Taoyuan large leaf tea which are widely planted in tea areas in Hunan, sequentially selecting tea leaves of one bud with two or three leaves or symmetric leaves with same tenderness, then performing ultraviolet irradiation, withering, making green, kneading, fermenting, drying, and enriching the fragrance on the selected leaves, wherein green making tea juice is respectively sprayed in the kneading and fermentation processes. By adopting the processing method, the defects that the leaves are not green, the taste is thin, the fragrance is poor, the color of tea soup is dark, the concentration intensity is poor, and the astringency is poor when a conventional fermentation process is adopted are overcome, the techniques of the process steps are all improved, the Congou black tea processed by using the processing method is uniform in fermentation, the leaf is bronze, the taste is mellow and fresh, the fragrance is heavy and long-lasting, the tea soup is red and right, and the astringency is high; the quality and the competitiveness of the Hunan medium/small leaf Congou black tea in the domestic and international black tea markets are remarkably improved.
Owner:HUNAN AGRICULTURAL UNIV

Residuum hydrotreatment-catalytic cracking combination technology

A residuum hydrotreatment-catalytic cracking combination technology of catalytic cracking recycle oil is characterized in that a material inlet is arranged in front of a metal removal agent bed layer, a desulfurizer bed layer, and a residual carbon removal agent bed layer of a device respectively, residuum and hydrogen enter the device to react through a device raw material port, hydrogenated residuum enters a catalytic cracking device and continuously reacts, one part of the recovery oil of the catalytic cracking device enters a hydrogenation device to react through one or more of four material inlets of a hydrotreatment device, and the residual recovery oil of the catalytic cracking device is cycled to the catalytic cracking device and enters the catalytic cracking device together with the hydrogenated residuum. The technology enables the operations of the residuum hydrotreatment-catalytic cracking combination technology to be flexible and efficient, and has the advantages of prolongation of the operation period of the residuum hydrotreatment device, improvement of the impurity removal rates of residuum hydrogenation products, reduction of the application amount of cold hydrogen, and increase of the yield of light oil having high added values.
Owner:PETROCHINA CO LTD

Method for preparing mesophase pitches or mesophase microspheres through coal and oil co-liquified residues

ActiveCN105036116AHigh content of mesophaseHigh aromaKeroseneMicrosphere
The invention provides a method for preparing mesophase pitches or mesophase microspheres through coal and oil co-liquified residues. The coal and oil co-liquified residues and a first-level extracting solvent are subjected to positive extraction, first-level extract liquor and first-level raffinate are obtained, remaining substances obtained after the first-level extracting liquid solvent is recycled are a mixture of asphaltene and heavy oil, the mixture of the asphaltene and the heavy oil and a second-level extracting solvent are subjected to position extraction, and second-level extract liquor and second-level raffinate are obtained; the second-level raffinate is processed, and asphaltene is obtained; heavy oil is obtained after the second-level extracting liquid solvent is recycled; the asphaltene and the heavy oil are mixed according to a certain proportion and evenly placed in a reactor to be subjected to co-carbonization thermal polycondensation, and thermal polycondensation products containing the mesophase pitches or thermal polycondensation products containing the mesophase microspheres are generated; the thermal polycondensation products containing the mesophase microspheres are washed through quinoline, filtered and dried, and the mesophase microspheres are obtained. The method has the advantages of being simple in technology and low in production cost.
Owner:TAIYUAN UNIV OF TECH +1

Roller drying machine

The invention discloses a roller drying machine, and belongs to the technical field of tea processing devices. The roller drying machine comprises a main frame, wherein a side plate and a top plate are fixedly arranged on the main frame, a roller is arranged in the main frame, and driven by a transmission mechanism arranged on the main frame, a heat source exchange chamber is arranged below the roller, an axial flow fan is arranged on one side of the heat source exchange chamber, a hot air pipe is arranged in the roller, the roller is sheathed with an electromagnetic heating jacket, a perforated closed plate is fixedly arranged at the feed end of the roller, a wet exhaust hood is sheathed at the discharging end of the roller, a wet exhaust fan is arranged at the upper end of the wet exhaust hood, a hot air inlet is formed in the lower end of the wet exhaust hood, the hot air pipe is connected with a hot air pipe interface arranged in the wet exhaust hood, the hot air pipe interface is communicated with the hot air inlet, and the hot air inlet faces to the axial flow fan. The roller drying machine disclosed by the invention simultaneously has the functions of green removing, roll drying and stir-frying, a product obtained by using the roller drying has jade green color and high fragrance which are better than that of the traditional stir-frying product and higher than that of a hot air dried product respectively.
Owner:宁波市姚江源机械有限公司

System device for producing needle coke crude oil through catalytic slurry oil

The invention belongs to the field of catalytic slurry oil deep processing and particularly relates to a system device for producing needle coke crude oil through catalytic slurry oil. According to the device, a mixer 1, the top of a catalytic slurry oil extraction tower 2, the top of an aromatic-hydrocarbon-rich oil separation tower 4 and the top of an aromatic-alkane-rich oil separation tower 5 are sequentially connected through pipelines. The bottom of the catalytic slurry oil extraction tower 2 is connected with a gas stripping tower A8-1. The bottom of the aromatic-hydrocarbon-rich oil separation tower 4 is directly connected with a gas stripping tower B8-2. The bottom of the aromatic-alkane-rich oil separation tower 5 is connected with a gas stripping tower C8-3. A gas outlet of the gas stripping tower A8-1, a gas outlet of the gas stripping tower B8-2 and a gas outlet of the gas stripping tower C8-3 are sequentially connected and then connected with a condenser 7 and a solvent tank 6, and the bottom of the gas stripping tower B8-2 is connected with a hydrofining reactor 9. The device fully utilizes petroleum resources and turns waste into wealth, the catalytic slurry oil can be utilized at high value, and the produced needle coke crude oil can serve as needle coke raw materials high-additional-value products.
Owner:GUANGXI HONGDA BIO ENERGY TECH

Method for efficiently preparing petroleum asphalt-based mesocarbon microbeads

The invention discloses a method for efficiently preparing petroleum asphalt-based mesocarbon microbeads. The method comprises the following steps: firstly, carrying out full mixing and preheating treatment on petroleum asphalt and an additive under a certain temperature, a certain N2 flow and a certain stirring speed, thus removing a small molecule compound which is difficult to polymerize; secondly, carrying out thermal polymerization reaction by keeping constant temperature for 2 to 6 hours under N2 protection and under the conditions that the pressure is 0.5 to 2.0 MPa and the temperatureis 380 to 420 DEG C, thus obtaining polymerized asphalt containing mesocarbon microbeads; finally, carrying out hot melting and filtration on the polymerized asphalt by using wash oil of which the boiling range is 245 to 290 DEG C, and carrying out vacuum drying after extracting filter cake by organic solvents of pyridine, methylbenzene and the like, thus obtaining the petroleum asphalt-based mesocarbon microbeads. According to the method disclosed by the invention, the petroleum asphalt and the additive which are used in the invention are rich in sources and lower in cost; by controlling themass percentage of the additive, the mesocarbon microbeads which are uniform in particle size distribution, controllable in size and relatively higher in yield can be prepared, and the mesocarbon microbeads can be used as lithium ion battery cathode materials after the mesocarbon microbeads are carbonized and graphitized.
Owner:INST OF PROCESS ENG CHINESE ACAD OF SCI
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