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349 results about "Drum drying" patented technology

Drum drying is a method used for drying out liquids from raw materials with a drying drum. In the drum-drying process, pureed raw ingredients are dried at relatively low temperatures over rotating, high-capacity drums that produce sheets of drum-dried product. This product is milled to a finished flake or powder form. Modern drum drying techniques results in dried ingredients which reconstitute immediately and retain much of their original flavor, color and nutritional value.

Production technique of three-dimensional curly hollow polyester staple fibers

The invention discloses a production technique of three-dimensional curly hollow polyester staple fibers, wherein the production technique comprises the steps of: utilizing regenerative PET material as raw material; sequentially performing the following procedures to obtain a finished product: pre-treating, drum drying, melting spinning, cooling forming, winding, stretching, curling, oiling, cutting and heat setting, wherein the drum drying duration is 9.5-10.5 h, a spinneret plate in the melting spinning procedure is three-dimensional hollow helical, the cross section of a spinneret orifice is a sealed space formed by sealing the circular arcs of two concentric circles, the temperatures of the threaded rod of a threaded rod extruding machine and the box body of a spinning box are 265-275 DEG C; a circular air blowing asymmetrical cooling forming mode is utilized, the circular blowing blast temperature is 20-24 DEG C, and the circular blowing wind speed is 4.7-5.7 m / s; the total stretching fold is 2.5-2.7 folds, the main curling pressure of a curling wheel is 0.05-0.1 MPa, and no backpressure exists; the heat setting temperature is 175-180 DEG C, and the heat setting duration is 10-14 min. The production technique of the invention has the advantages of saving the cost and protecting the environment, and the prepared finished product not only has good three-dimensional configuration and bulkiness, but also has better thermal stability.
Owner:HANGZHOU BEST CHEM FIBER

Method for regulating multi-site processing intensity uniformity of in-process products in tobacco drum drying process

ActiveCN106690391AAvoid Control InaccuraciesLow costTobacco preparationMulti siteMonitoring system
The invention relates to a method for regulating multi-site processing intensity uniformity of in-process products in tobacco drum drying process. The method is characterized by comprising the following steps of enabling a tobacco material drum heat and damp treatment online monitoring system to detect the axial temperature distribution of the in-process product in the drum; according to the data, enabling a programmable controller and a computer to calculate and determine the processing intensity of the in-process product in the drum drying equipment; by using the uniformity control of the processing intensity index of the in-process product as the criteria at the original processing site, detecting and calculating the processing intensity of the in-process product in the drum equipment at the foreign processing site, sequentially changing the hot wind temperature and cylinder wall temperature of the foreign processing site, and adjusting the processing intensity index to be not obviously different from the processing intensity of the original processing equipment, so as to obtain the uniform processing condition. The method has the advantages that the defect of difficulty in guaranteeing of the quality of the multi-site processing product is overcome; the technological parameters are regulated according to the processing intensity value, so as to finally reach the purposes of improving processing intensity uniformity of the tobacco material, and stabilizing the quality of a cigarette product.
Owner:ZHENGZHOU TOBACCO RES INST OF CNTC

Tobacco roller far infrared composite dying experimental equipment

Provided is tobacco roller far infrared composite dying experimental equipment. The tobacco roller far infrared composite dying experimental equipment is characterized by comprising a horizontal roller, a hot air conveying system connected with the roller and a far infrared heating device arranged in an inner cavity of the roller. The hot air conveying system comprises an air source, an air preheater, a steam generator, a heat exchanger and an air conveying pipeline communicated with the inner cavity of the roller, and the air source, the air preheater, the steam generator, the heat exchanger and the air conveying pipeline are connected in sequence. A material opening is formed in the rear end wall of the roller, and a moisture discharge pipe is arranged. According to the experimental equipment, roller wall heat conduction heating, hot air convection heating and far infrared radiation heating in traditional cut tobacco roller drying are combined. A plurality of heating modes are combined, the cut tobacco can be dried fast at low roller wall temperature, and products with even moisture and the good filling effect are obtained. The roller wall temperatures and far infrared radiation strength of different roller drying stages are controlled according to different raw materials and different product targets, and then differentiation production and fine production are achieved.
Owner:ZHENGZHOU TOBACCO RES INST OF CNTC

Grain screening and drying device for agriculture

The invention discloses an agricultural grain screening and drying device, which comprises a drying chamber, a limit chute is symmetrically arranged on the left and right side walls of the drying chamber, a drying screen cylinder is horizontally arranged in the drying chamber, and a right end of a rotating nozzle is provided. A limit bearing seat is sleeved; a horizontal plate is arranged on the drying chamber, a left vertical plate and a right vertical plate are symmetrically arranged on the horizontal plate, a driving device is installed on the elliptical cam, and left limit plates are respectively arranged on the left and right sides of the elliptical cam and the right limit plate, the bottom ends of the left limit plate and the right limit plate are both provided with guide sliders slidingly connected with the horizontal plate; both ends of the screen plate extend to the outside of the drying chamber, the first extension plate and the second extension plate The bottom surface is provided with a boom, and the boom is rotatably provided with a swing rod. The structure of the invention is ingenious. The rotating nozzle is driven by the driving motor and drives the stirring block to turn and stir the grains, so that the grains are more dispersed. The jetted hot air dries the grains by wind, which greatly improves the drying effect of the grains.
Owner:张宇霞

Rice product rich in gamma-aminobutyric acid and method for producing the same

The invention belongs to the technical field of rice deep processing, in particular to a production method of a functional rice product which has a special sweet flavor and is rich in Gamma-aminobutyric acid and a product thereof, the rice product is produced by virtue of the activities of high glutamate decarboxylase, amylase and protease in germinated brown rice of an indica type rice or a non glutinous rice. The invention takes the indica type rice or the non glutinous brown rice as a raw material which carries out the steps of cleaning, disinfection, soaking, germination, cleaning, beating into rice milk, heat insulation, transformation, drum drying or spray drying, and the like, to be produced into functional nutrition rice flake or rice powder which is rich in Gamma-aminobutyric acid. Compared with the prior art, the rice product makes full use of the activities of the glutamate decarboxylase, the amylase and the protease in the germinated brown rice; the produced rice product has the special sweet flavor; by calculating based on dry basis, the content of Gamma-aminobutyric acid is high (1,000-1,400mg/100g), and the nutritional value and the digestibility are high. The rice product of the invention can be taken as the functional food for resisting fatigue and reducing blood lipid.
Owner:HUAZHONG AGRI UNIV

Production process for coloured polyester staple fibre

The invention discloses a production process for coloured polyester staple fibre. In the production process, regenerative PET (Polyethylene Terephthalate) material is used as the raw material, and the finished product is acquired by pre-treating, rotary drum drying, melt spinning, cooling forming, winding, drafting, curling, oil applying, thermosetting and cutting-off in sequence, wherein the rotary drum drying comprises the steps of firstly drying the regenerative PET material for 7.5h-8.5h and then adding master batches with the final mass fraction of 2%-10%, and toner; the total drying time is 9.5h-10.5h; both the screw rod and the spinning beam of a screw extruder in the melt spinning step are at the temperature from 265 DEG C to 275 DEG C; spinneret plates are provided with 3500 bores having the diameter of 0.2mm and are arranged in 14 circles; cooling forming is realized through circular air blow, the temperature of the circular air is 22 DEG C to 26 DEG C, and the velocity of the circular air is 4.0m/s to 5.0m/s; the total draft multiple is 3.0-3.2 times; and the thermosetting temperature is 168 DEG C to 172 DEG C, and the thermosetting time is 13 minutes to 17 minutes. Theproduction process can save the cost and is helpful for environmental protection; the produced product has smaller linear density, higher colour fastness and smooth and comfortable hand feeling.
Owner:HANGZHOU BEST CHEM FIBER

Novel production process for cut tobacco stems

The invention discloses a novel production process for cut tobacco stems. The novel production process comprises the steps as follows: carrying out vacuum moisture regaining and evaporating the stems; storing the stems; heating and humidifying; straightening the stems; pressing the stems; arranging the stems; cutting the stems; feeding; expanding and drying; and perfuming. According to the novel production process, the vacuum moisture regaining and stem evaporating mode is adopted for moisture regaining of the tobacco stems, so that the impurity gases in the tobacco stems can be removed and the smoke softness is improved. The thinly pressing and cutting mode is adopted, so that the physical forms of the formed cut stems are threadlike and are closer to cut tobaccos. The flash evaporation, expansion and drum drying mode is adopted for drying of the cut stems, so that the cut stems are better in crimpiness and are closer to the form of the cut tobaccos and the filling capability of the cut stems can be improved. The cut steams produced by the production process has the advantages that the filling value is high, the impurity gases in the tobacco stems are reduced, the fragrance is increased, cigarettes can be endowed with a certain burned sweet fragrance, the physical forms of the cut stems are closer to the cut tobaccos, and the suitability is better in the cigarettes.
Owner:YUNNAN REASCEND TOBACCO TECH GRP

Flame-resistant and antibacterial polyester staple fiber and production technique thereof

The invention discloses a flame-resistant and antibacterial polyester staple fiber and a production technique thereof; the flame-resistant and antibacterial polyester staple fiber is prepared by soaking terylen protofilament, spraying flame-resistant and antibacterial aqueous emulsion in multiple angles and drying; the flame-resistant and antibacterial aqueous emulsion is prepared by mixing a Galston Lurol PS-9985 oiling agent, a Galston Lurol AM-7 antibacterial agent and tri-distilled water. The production technique comprises the steps of: utilizing regenerative PET material as raw material;sequentially performing the following procedures to obtain a finished product: pre-treating, drum drying, smelting and spinning, cooling forming, winding, stretching, curling, oiling, cutting and heat setting, wherein the drum drying duration is 9.5-10.5 h, the temperatures of the threaded rod of a threaded rod extruding machine and the box body of a spinning box are 265-275 DEG C; the total stretching fold is 3.5-4.0 folds, the heat setting temperature is 140-150 DEG C, and the heat setting duration is 8-12 min. The production technique of the invention has the advantages of saving the cost,protecting the environment, simultaneously performing the flame-resistant and antibacterial treatment, and simplifying the steps, and the prepared finished product not only has excellent flame-resistant and antibacterial performance, but also has a long effect.
Owner:浙江华顺科技有限公司

Household garbage coupling fluidized bed grading pyrolysis gasification technology

ActiveCN102936518ASolving the fly ash problemEliminate dioxinsGranular/pulverulent flues gasificationHeat carrierSlag
The invention provides a household garbage coupling fluidized bed grading pyrolysis gasification technology. Household garbage is firstly subjected to deferrization and crushing, then 0-6mmgarbage particles are dried through a casing pipe type rotary drum drying machine, garbage particles and a small quantity of heat carriers are sent to the middle lower portion of an entrained flow reactor to be mixed with gasified gas and circulating ash and lifted up to be performed with hydroforming pyrolysis, after gas-solid separation, first-stage separated high-temperature coarse semi-coke return to the bottom of a coupling fluidized bed to react between 800-1000 DEGC to generate gasified gas, and the gasified gas and the circulating ash together to flow upwards to form material circulation. Second-stage separated high-temperature fine semi-coke is sent to an entrained-flow bed to react between 1200-1600 DEG C to generate high-temperature gas, and the high-temperature gas and liquid ash slag simultaneously flow out of the entrained-flow bed in spiral inclined-downwards mode, and the high-temperature gas go upwards and enter the coupling fluidized bed. The liquid ash slag flows downwards to a circulating ash material layer of a circulating fluidized bed and is subjected to heat exchange to be solidified into solid ash slag. Combustion gas separated from the second stage servers as product gas to be supplied externally.
Owner:CHINA UNIV OF PETROLEUM (EAST CHINA)

Velveteen regeneration polyester super-short fiber and production technique thereof

The invention discloses velveteen regeneration polyester super-short fiber and production technique thereof. The velveteen regeneration polyester super-short fiber is prepared from regenerative PET materials by raw material pre-treatment, rotary drum drying, melt spinning, cooling forming, wire placing barrel falling after winding, bundling, drafting, curling, oiling, heat setting and cutting to obtain the product fiber. According to the production technique of the invention, the velveteen regeneration polyester super-short fiber can save cost, protect environment and further ensure the product quality and further prevent the super-long and over-length fibers from being generated in the production process; the cut length of the obtained product is uniform and precise and controlled within 3 to 12mm and the product has the similar appearance and hand feel similar to the down. The velveteen regeneration polyester super-short fiber has smooth hand feel and ideal down filling effect; the suitable fiber length of the velveteen regeneration polyester super-short fiber is convenient for the downstream producers to realize the fully-automatic filling, improve the production efficiency and have higher cost performance in compared with the super-short fiber spun by the raw material.
Owner:HANGZHOU BEST CHEM FIBER

Production process for flame retardant polyester staple fibre

The invention discloses a production process for a flame retardant polyester staple fibre. In the production process, regenerative PET (Polyethylene Terephthalate) material is used as the raw material, and the finished product is acquired by pre-treating, rotary drum drying, melt spinning, cooling and forming, winding, drafting, curling, oil applying, thermosetting and cutting-off in sequence, wherein the rotary drum drying comprises the steps of firstly drying the regenerative PET material for 7.5h-8.5h and then adding flame retardant chips with the final mass fraction of 6%-8%; the flame retardant chips are halogen-free flame retardant copolyester chips, and the total drying time is 9.5h-10.5h; both the screw rod and the spinning beam of a screw extruder in the melting spinning step areat the temperature from 268 DEG C to 278 DEG C; spinneret plates are provided with 3500 bores having the diameter of 0.2mm and are arranged in 14 circles; cooling forming is realized through circularair blow; the total draft multiple is 2.7-2.9 times; and the thermosetting temperature is 168 DEG C to 172 DEG C, and the thermosetting time is 13 minutes to 17 minutes. The production process can save the cost and is helpful for environmental protection; the produced product has a smaller linear density, a higher limited oxygen index and good flame retardant effects.
Owner:HANGZHOU BEST CHEM FIBER

Countercurrent double-loop cylinder dryer

The invention relates to a countercurrent double-loop cylinder dryer, which comprises a support, an inner cylinder, an outer cylinder, a driving device, a feeding device and a discharging device, and is characterized in that: a middle cylinder is arranged between the inner cylinder and the outer cylinder, and one end of the inner cylinder and one end of the middle cylinder are respectively provided with an annular seal plate; one end of the outer cylinder is provided with a seal plate, and the three cylinders constitutes a material layer and two flue gas heating units, i.e., an inner-layer flue and an outer-layer flue; and a plurality of reinforcing supporting columns are arranged among the three cylinders for connecting and positioning, and frying plates are uniformly arranged on the outer wall plate of the inner cylinder and the inner wall plate of the middle cylinder. The problems that the material and the flue gas flow from the same pipeline, and are fully mixed, so that the dried material is mixed with impurities and the production safety is possibly generated by ineffectively controlling sparks in the flue gas to be contacted with the material and the like in the traditional drum drying machine can be solved, the structural design is reasonable, the performance is stable, the process flow is smooth, the overheating time of a dry area is long, the thermal efficiency is high, the energy is saved and the consumption is reduced, the quality of the dried material is high, and the range of application is wide.
Owner:NANNING ZHONGXIU ENERGY SAVING ENVIRONMENTAL PROTECTION ENG

Purple sweet potato cooked whole flour production line

The invention provides a purple sweet potato cooked whole flour production line, which mainly consists of a cyclone stone removing cleaning machine, a cage type cleaning machine, a weighing instrument, a rotary steam peeling machine, a peel brushing cleaning machine, a quality inspection conveyor, a slicing machine, a blanching machine, a cooling machine, a steaming and boiling machine, a paste preparing machine, a rotary drum dryer, a diaphragm crushing machine, a sieving machine, a packaging machine and the like, wherein conveyors or pumps are arranged between the devices and connect the devices to form the production line. The purple sweet potato cooked whole flour production line has the advantages that under the condition of not using any chemical synthetic agents, purple sweet potato cooked whole flour with stable quality can be safely, sanitarily and continuously produced in a large scale; the reconstitution property of the product is good; in addition, more nutritious ingredients can be maintained in the product, so the flavor and the mouthfeel are more similar to those of fresh purple sweet potatoes; in addition, the equipment configuration is economic and reasonable; the operation reliability is high; the maintenance cost is low; and the automation degree is high.
Owner:东台市食品机械厂有限公司

Tartary buckwheat tea and preparation technology thereof

The invention discloses a tartary buckwheat tea and a preparation technology thereof. The tartary buckwheat tea is composed of 500 parts to 800 parts of tartary buckwheat cortex powder, 50 parts to 100 parts of tartary buckwheat extractives and 50 parts to 80 parts of green tea powder. The preparation technology of the tartary buckwheat tea includes steps of powder mixing, molding, drying and fragrance improving, the tartary buckwheat cortex powder, the tartary buckwheat extractives and the green tea powder are mixed uniformly until the color is uniform, and the mixture is stood for 20 minutes; uniformly mixed green tea is taken, 25% to 30% of water is added, the mixture is mixed uniformly by a pressurization molding machine and subjected to 30 meshes to be granulated; molded tartary buckwheat granules are placed in a plate and then in a hot air drying box, the granules are dried at a temperature ranging from 50 DEG C to 55 DEG C until the water content is less than 8%, then the dried granules are placed in a far infrared oven to be baked at a temperature ranging from 200 DEG C to 220 DEG C for 2 to 3 minutes and then cooled naturally; and the cooled tartary buckwheat tea is placed in a roller drying oven to be baked at a temperature ranging from 110 DEG C to 145 DEG C until the water content is no more than 5%.
Owner:太原市素有苦荞食品有限公司

Drying plant for high-moisture percentage plaster pasty materials

The invention discloses a device for drying paste-shaped materials with high water content, which belongs to the technical field of drying. The device is characterized by mainly comprising a feed system, a dry system, a discharge system and a tail gas treatment system. The dry system comprises a steam boiler, a revolving drum type pressed film sludge drier, a heat exchanger, a forming machine and a secondary drier. The material is input into the revolving drum type drier through the feed system and is extruded and formed in the forming machine after drying; the formed material is dried through hot wind at a vertical interface so that the surface is encrusted; and the encrusted sludge is superposed in the secondary drier introduced with hot air for drying. One part of the dried sludge serves as the fuel for the steam boiler and is burnt to generate steam, while the other part is conveyed to a cylindrical silo directly. The condensed water discharged by the revolving drum type drier is heated into air by the heat exchanger and is introduced into the revolving drum type drier to serve as a drying medium and a water vapor carrying medium. Dried tail gas enters the tail gas treatment system and is discharged after the treatment. The device has the advantages of high drying efficiency for the whole set of the dry system, small generation of pollution and achievable automatic operation.
Owner:DALIAN UNIV OF TECH

Method for drying tobacco shreds

The invention relates to a method for drying tobacco shreds, and belongs to the technical field of tobacco processing. The method for drying the tobacco shreds comprises tobacco shred hyper transport (HT) tunnel type heating and humidifying pretreatment, rotary drum drying stage and microwave drying and shaping stage. HT tunnel type heating and humidifying equipment, rotary drum drying equipment and a control system which are adopted by the method are all purchased from the market, wherein microwave drying equipment which is purchased from the market is reconstructed, microwave magnetrons with ultrahigh frequency (2450 megahertz) and monotube miniwatt (1.5 kilowatts) are adopted instead and are controlled in group, and a rotary drum conveying mode is adopted. The method adopts the combination of two drying modes, and the extensive drying and fine drying of the tobacco shreds are sequentially combined; the method has the advantages that the tobacco shreds are dried and expanded uniformly, and have stable quality; the adverse effects which are caused to the aroma and quality of the tobacco shreds during the conventional high-temperature drying process are effectively solved, so that the purposes of improving the quality and increasing the aroma are realized; and the tobacco shreds are stably shaped, and are high in filling value and good in processing resistance.
Owner:YUNNAN RES INST OF TOBACCO SCI

Composite modified starch and preparation method thereof

InactiveCN110204624AWater retention and anti-agingShear resistantDrum dryingSlurry
The invention discloses a preparation method of composite modified starch. The preparation method comprises the following steps: (1) blending a starch slurry: uniformly stirring water, an expansion inhibitor and native starch to obtain the starch slurry; (2) performing an etherification reaction: adding an etherifying agent to carry out the etherification reaction; (3) performing a crosslinking reaction: adding a crosslinking agent, and carrying out the reaction to reach a desired viscosity; (4) adjusting the pH value of a reaction solution obtained after the crosslinking reaction in step (3)with an inorganic acid solution, adding an esterification agent, carrying out a reaction for 3 h, and then terminating the reaction to obtain the composite modified starch; ad (5) washing and dehydrating the composite modified starch prepared in step (4), and carrying out drum drying to obtain the product. The composite modified starch of the invention is obtained by etherification, the crosslinking reaction and the esterification reaction of the native starch, and the single product can meet the application requirements without being combined with other starches. The preparation method of thecomposite modified starch of the invention has the advantages of easily controlled process conditions, easiness in realization of large-scale industrial production, easiness in operation, and strongpracticability.
Owner:HENAN HENGRUI STARCH TECH CO LTD

Production process for bamboo charcoal polyester staple fibre

The invention discloses a production process for a bamboo charcoal polyester staple fibre. In the production process, regenerative PET (Polyethylene Terephthalate) material is used as the material, and the finished product is acquired by pre-treating, rotary drum drying, melt spinning, cooling and forming, winding, drafting, curling, oil applying, thermosetting and cutting-off in sequence, wherein the rotary drum drying comprises the steps of firstly drying the regenerative PET material for 5.5h-6.5h and then adding bamboo charcoal master batches with the final mass fraction of 6%-8% and including bamboo charcoal with the mass fraction of 22%-27%; and the total drying time is 9.5h-10.5h; both the screw rod and the spinning beam of a screw extruder in the melt spinning step are at the temperature from 278 DEG C to 282 DEG C; cooling forming is realized through circular air blow, the temperature of the circular air is 22 DEG C to 26 DEG C, and the air velocity of the circular air is 4.0m/s-5.0m/s; the total draft multiple is 3.1-3.3 times; and the thermosetting temperature is 162 DEG C to 168 DEG C, and the thermosetting time is 13 minutes to 17 minutes. The production process can save the cost and is helpful for environmental protection; the produced product has a better smooth and comfortable hand feeling and moisture-absorption air permeability than those of a normal polyester staple fibre.
Owner:HANGZHOU BEST CHEM FIBER
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