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37results about How to "Extended spin time" patented technology

Manufacturing method of paraffin sections of zostera marina embryo

The invention discloses a manufacturing method of paraffin sections of zostera marina embryo, comprising the following steps: (1) material drawing and fixation: zostera marina seeds are taken and the fruit skin is stripped, and after endosperm is removed, an integral zostera marina embryo is soaked in FAA (free amino acids) fixing solution and is fixed for more than 48 hours; (2) dehydration: the zostera marina embryo is taken out from the fixing solution and is soaked in alcohol for dehydration; (3) waxing and embedding: paraffin is added gradually in a vessel containing the zostera marina embryo and dimethylbenzene, and conventional paraffin embedding is carried out to obtain the wax blocks containing the zostera marina embryo; (4) slicing, spreading and drying: the wax blocks coated with the zostera marina embryo is fixed on a wheel rotation type slicing machine for carrying out continuous slicing of the paraffin, so as to obtain wax bands and enable the wax bands to be attached to an object slide; (5) dewaxing, rehydration and dyeing of hematoxylin dye solution; (6) slicing, dehydration and dyeing of eosin and alcohol; and (7) transparence and mounting are carried out to manufacture a permanent section. In the manufacturing method disclosed by the invention, the paraffin sections of the zostera marina embryo, which have clear dyeing and an integral texture structure, can be obtained.
Owner:SHANDONG ORIENTAL OCEAN SCI TECH

Quick electrostatic agglomerate separating device and process

ActiveCN103343017ASolve low dehydration rateSolve the problem of oily drainageDewatering/demulsification with electric/magnetic meansHigh energyTransformer
The invention provides a quick electrostatic agglomerate separating device and a quick electrostatic agglomerate separating process. The quick electrostatic agglomerate separating device is composed of a pry seat, an oil-water separation tank, an oil-water interface instrument, a water outlet, a gas-liquid separation tank, a liquid inlet, a gas outlet, a pressure gauge, a gas-liquid interface instrument, an adsorption plate, a water outlet, an oil/water transmission pipe, an oil outlet, a transformer, a transformer, a control cabinet, a high pressure introduction hole, a feed oil distributor, an electrostatic coalescence electrode and a discharged oil collecting pipe; a high water cut well liquid enters the gas-liquid separation tank via the liquid inlet; a combustible gas is discharged from the gas outlet and enters the oil-water separation tank; oil and water are separated from each other under the action of gravity, and further separated in an electric field generated by the electrostatic coalescence electrode; and crude oil is output from the oil outlet. Therefore, the problems of low crude oil dehydration rate, high oil content in drainage and high energy consumption are solved, the electric field space is extended and the dehydration time of crude oil in the electric field is prolonged; and as the result, the dehydration efficiency is effectively improved, the electricity consumption in operation is reduced and the production cost is reduced.
Owner:LUOYANG ZHENGYUAN PETROCHEM

Melt/solid state polycondensation preparation method for polylactic acid

ActiveCN102040730ASmall molecular weightShort molecular weightLactideReaction temperature
The invention relates to a melt/solid state polycondensation preparation method for polylactic acid, which mainly solves the problems of long reaction time, difficult continuous production or high cost in the prior art. The method comprises the following steps of: 1) performing a dehydration oligomerization reaction of lactic acid at the temperature of between 100 and 160 DEG C under the absolute pressure of between 6,000 and 25,000 Pa and under the action of a catalyst A for 0.5 to 5 hours first, and continuing the ehydration oligomerization reaction at the temperature of between of 120 and 180 DEG C under the absolute pressure of between 200 and 1,500 Pa and under the action of the catalyst A for 0.5 to 5 hours to generate a product I; 2) performing a melt polycondensation reaction of the product I at the reaction temperature of between 150 and 200 DEG C under the absolute pressure of between 30 and 600 Pa and under the action of a catalyst B for 0.5 to 15 hours to generate a polylactic acid prepolymer and lactide serving as a by-product, and refluxing the lactide to a reaction mixture at the reflux temperature of between 70 and 95 DEG C; 3) pelletizing the polylactic acid prepolymer obtained in the step 2), and crystallizing in an inertia airflow at the temperature of between 50 and 130 DEG C for 0.5 to 10 hours; and 4) performing a solid state polycondensation reaction of the polylactic acid prepolymer processed in the step 3) in the inertia airflow at the temperature of between 120 and 170 DEG C for 5 to 40 hours to obtain the polylactic acid. The technical scheme of the invention better solves the problem, and can be used for the industrial production of the polylactic acid.
Owner:CHINA PETROLEUM & CHEM CORP +2

Tank field temperature maintaining and rising system

InactiveCN105329568AReduce energy consumption and production costsSpeed up dehydration timeLarge containersTank wagonsEngineeringEnergy consumption
The invention discloses a tank field temperature maintaining and rising system which comprises at least one storage tank, wherein the storage tank is connected with a material inlet pipeline and a material outlet pipeline respectively; a temperature maintaining pipeline is connected onto the material outlet pipeline; a heat exchanger is connected onto the temperature maintaining pipeline; part of material flows into the temperature maintaining pipeline via the material outlet pipeline and then flows into the material outlet pipeline via the temperature maintaining pipeline after heat exchange and temperature rise by the heat exchanger. According to the invention, the temperature maintaining pipeline and the heat exchanger arranged outside the storage tank can heat part of the material and mixes part of the material with the unheated material in the storage tank to further realize temperature maintenance and rise of the material in the storage tank and replace the original heating and temperature maintenance manner through steam; in addition, hot water (technological waste heat) is adopted to maintain the temperature of the storage tank and heat the storage tank, so that the steam use level is decreased, and the production cost and energy consumption are reduced; through filling a demulsifier, the material dehydration time is shortened, and the dehydration effect is improved; the heating manner outside the storage tank is adopted to reduce the maintenance cost when the existing heating coil in the storage tank leaks.
Owner:GUANGZHOU YOUHUA PROCESS TECH

Pectin dedicated volute sludge dehydrator and screw shaft thereof

The invention discloses a pectin dedicated volute sludge dehydrator and a screw shaft thereof. A reducing variable pitch screw shaft is adopted, a pitch of a screw panel is gradually reduced along a sludge outlet tank; the diameter of the screw shaft is gradually increased along a sludge outlet tank direction from the 1 / 3 position of the shaft length; and the length of the back 2 / 3 section of the screw shaft, namely the dehydration section, is increased by 10-15%. Aiming at the features that the pectin is high in sludge organic content, soft in mud, light in proportion, and hard to dehydrate, the pectin dedicated volute screw shaft is innovated and designed; and through special design of the screw shaft, the pressure in a dehydration cavity is higher, the compression ratio of a mud inlet end to a mud outlet end can achieve 3.5: 1, the dehydration time is longer, and the dehydration effect is better. The pectin dedicated volute sludge dehydrator has the characteristics of being larger in cavity pressure, hard to stick the shaft, longer in sludge dehydration retention time and high in dehydration efficiency; and the sludge dehydration effect can be effectively improved while guaranteeing that the processing efficiency of unit time cannot be reduced.
Owner:SHANGHAI TECHASE ENVIRONMENT PROTECTION

Taro powder making device

The invention belongs to the technical field of agricultural product processing, and particularly relates to a taro powder making device. In order to solve the problems in the prior art, the followingscheme is provided: the taro powder making device comprises an outer cylinder body, wherein a feeding hopper is arranged on the outer wall of the top of the outer cylinder body, and a feeding cover covers the outer wall of the top of the feeding hopper; a material distributing plate is fixedly connected to the inner wall of the side surface of the outer cylinder body through a connecting rod, anda conical shell is fixedly connected to the inner wall of the side surface of the material distributing plate; a material extruding shell is fixedly connected to the outer wall of the top of the material distributing plate, and material extruding openings which are annularly and uniformly distributed are formed in the bottom of the outer wall of the side surface of the material extruding shell; and a screen is fixedly connected to the inner wall of the bottom of the outer cylinder body. According to the taro powder making device disclosed by the invention, the working procedure of making taropowder can be omitted, the efficiency of making the taro powder is improved, the temperature in the outer cylinder body can be reduced, pasty taros are prevented from being adhered to the inner wallof the outer cylinder body and a cutter strip, the circumstance that the pasty taros on the screen are accumulated, and falling of the taro powder is influenced can be avoided, the dehydrating time ofthe pasty taros on the material distributing plate is prolonged, and the dehydrating efficiency is improved.
Owner:贲伟

Drum type washing machine and drum type washing and drying machine

By attaching the laundry to the unbalanced side in the low-speed rotation region of the spin-drying process, it is possible to shorten the correction time of the imbalance when large-sized clothes such as a carpet and a felt having different combinations are combined, and to provide a drum type washing machine and a drum type washing and drying machine that suppress the increase in the dehydrationtime and the amount of power consumption. The drum type washing machine comprises: a rotatable drum which is horizontally inclined or inclined in a manner that the depth side is downward; an outer tub which encloses the drum and is used for storing washing water; a casing which encloses the outer tub; a judging means and an imbalance determining means which judge the attaching state of the laundry in the rotatable drum ad the imbalance determination of the laundry in the first dehydrating operation. The first dehydrating operation is performed when the imbalance is greater than the thresholdof the imbalance determining means during the determination of the attachment state of the laundry. The rotation control of the dehydration operation after the second dehydration is started again, andthe rotation control of the second and subsequent dehydration operations is different from the dehydration operation.
Owner:HITACHI APPLIANCES INC

Vibrating-dewatering screen

The invention discloses a vibrating-dewatering screen. The vibrating-dewatering screen comprises a fixing base and a machine frame, wherein a spring shock absorption device is arranged on the fixing base; the machine frame is mounted on the fixing base through the spring shock absorption device; the spring shock absorption device comprises a shock absorption support and springs, wherein the springs are mounted on the shock absorption support, and a discharge opening is formed in the front end of the machine frame; a feeding hopper is arranged at the upper part of the rear section of the machine frame; and a liner is mounted at the top of the machine frame through a fixing shaft. Two vibrating motors arranged on the machine frame drive a screen mesh group to vibrate horizontally and vertically so as to dehydrate materials, the screen mesh group consists of three layers of screen clothes, meshes of the first screen cloth on the top layer are the biggest, materials of different specifications are vibrated to dehydrate on the different screen clothes, so that working procedures for subsequent working namely screening the materials are simplified, the processing time is shortened, and the production efficiency is improved. The screen mesh groups are obliquely placed, so that the dehydration time of the materials is prolonged, and more thorough dehydration is guaranteed.
Owner:LAIAN COUNTY XINYUAN MECHANICAL & ELECTRICAL EQUIP

Encryption case standby device based on human body activity charging

The invention provides an encryption case standby device based on human body activity charging. The device comprises a box body, and a treading plate is rotationally connected to the inner bottom wallof the box body; the outer side of the rotating shaft is fixedly sleeved with a bevel gear, the inner wall of the lifting base is provided with a rack corresponding to the bevel gear, the top of thelifting base is fixedly connected with a vertical plate, a lever plate is movably installed in the box body and located between the treading plate and the vertical plate, and a charging assembly corresponding to the storage battery is fixedly installed on the back face of the rotating shaft. When a user works, the treading plate is continuously treaded, deflection of the treading plate is continuously generated, the treading plate drives the vertical plate and the lifting base to move up and down through the lever plate; the lifting base drives the bevel gear and the one-way rotation through the rack, and the rotating shaft drives the conductor to rotate, so that magnetic induction lines between the magnet assemblies are cut, an induced current is generated, the storage battery is charged,the power storage capacity of the storage battery can be effectively ensured, and the left side work of the case is further ensured.
Owner:杭州雅凇科技有限公司

Front-loading washing machines and front-loading washer-dryers

By attaching clothes while correcting the imbalance in the low-speed rotational speed range of the dehydration process, it is possible to shorten the unbalance correction time of large garments such as blankets, or when combining blankets of different materials, and provide a front-loading washing machine that suppresses increases in dehydration time and power consumption. and a tumble washer dryer. It includes: a rotatable drum whose rotation axis is horizontal or inclined with the depth side at the bottom; an outer tub that encloses the drum and is used to store washing water; a shell that encloses the outer tub; judges the laundry in the drum The judging mechanism of the attached state and the imbalance judging mechanism of the first dehydration operation carry out the judgment of the attached state of the clothes and the judgment of the imbalance, and when the imbalance is greater than the threshold value of the imbalance judging mechanism, according to the first time The rotation control of the second and subsequent dehydration operations to restart dehydration is set based on the determination of the attached state of the clothes in the dehydration operation, and the rotation control of the second and subsequent dehydration operations is different from the first dehydration operation.
Owner:HITACHI GLOBAL LIFE SOLUTIONS INC

Melt/solid state polycondensation preparation method for polylactic acid

ActiveCN102040730BSmall molecular weightShort molecular weightLactideReaction temperature
The invention relates to a melt / solid state polycondensation preparation method for polylactic acid, which mainly solves the problems of long reaction time, difficult continuous production or high cost in the prior art. The method comprises the following steps of: 1) performing a dehydration oligomerization reaction of lactic acid at the temperature of between 100 and 160 DEG C under the absolutepressure of between 6,000 and 25,000 Pa and under the action of a catalyst A for 0.5 to 5 hours first, and continuing the ehydration oligomerization reaction at the temperature of between of 120 and 180 DEG C under the absolute pressure of between 200 and 1,500 Pa and under the action of the catalyst A for 0.5 to 5 hours to generate a product I; 2) performing a melt polycondensation reaction of the product I at the reaction temperature of between 150 and 200 DEG C under the absolute pressure of between 30 and 600 Pa and under the action of a catalyst B for 0.5 to 15 hours to generate a polylactic acid prepolymer and lactide serving as a by-product, and refluxing the lactide to a reaction mixture at the reflux temperature of between 70 and 95 DEG C; 3) pelletizing the polylactic acid prepolymer obtained in the step 2), and crystallizing in an inertia airflow at the temperature of between 50 and 130 DEG C for 0.5 to 10 hours; and 4) performing a solid state polycondensation reaction of the polylactic acid prepolymer processed in the step 3) in the inertia airflow at the temperature of between 120 and 170 DEG C for 5 to 40 hours to obtain the polylactic acid. The technical scheme of the invention better solves the problem, and can be used for the industrial production of the polylactic acid.
Owner:CHINA PETROLEUM & CHEM CORP +2

Method of extracting krill oil by supercritical CO2

The invention provides a method of extracting krill oil by supercritical CO2. The method comprising the steps of carefully selecting 100 to 300 parts of high quality krill meat; putting the well-selected high quality drill meat into water for heating, wherein the heating temperature is 55 to 85 DEG C, and the heating time is 5 to 15min; performing drying treatment on the heated krill meat, the drying temperature is 55 to 75 DEG C, and the drying time is 10 to 20min; smashing the dried krill meat into krill powder; putting the smashed krill powder into an extraction kettle, taking the supercritical CO2 as an extraction agent and taking methyl alcohol and ethyl alcohol as an entrainer, performing extraction, and the krill oil is obtained after extracting for 1 to 3 hours; the reaction of the supercritical CO2 and the krill powder is more perfect, the adding proportion of the methyl alcohol and the ethyl alcohol of the entrainer is 2 to 1 and the extraction rate is increased, the solubility and the selectivity of the supercritical CO2 are improved, the work efficiency is improved, and the method of extracting krill oil by the supercritical CO2 is suitable for large-scale industrialized production, simple in extraction method and extraction process step, easy to operate, low in component, and the extracted krill oil can meet the requirements of manufacturers.
Owner:JIANGSU JIANGDAYUAN ECOLOGICAL BIOLOGICAL TECH
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