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37results about How to "Fully distilled" patented technology

Distillation device for Baijiu

The invention discloses a distillation device for Baijiu. The distillation device is characterized in that a steam disperser is fixed at the center of the bottom of a steam tank, a motor is arranged on the outer wall of a steamer, a rotary shaft is connected to the motor, a first gear is fixedly connected to one end of the rotary shaft, a first steam inlet pipe is horizontally rotatably connected into the steamer, two ends of the first steam inlet pipe penetrates the lateral walls of the steamer and extend out of the steamer, the first steam pipe is provided with a plurality of stainless-steel stirring shafts, the stirring shafts are in clearance fit with the bottom of the steamer, one end of the steam inlet pipe is fixedly connected with a second gear in a sleeved manner, the first gear meshes with the second gear, the other end of the first steam inlet pipe is communicated with a second steam inlet pipe, the first steam inlet pipe is rotatably connected with the second steam inlet pipe, one end of the second steam inlet pipe is located in the steam tank and located above the steam disperser, and the steam tank is provided with a steam outlet pipe. When the distillation device is used for brewing the Baijiu, raw materials in the steamer can be thoroughly distilled, and distillation efficiency is increased at the same time.
Owner:ZUNYI JINHONG METAL EQUIP

Multifunctional volatile oil distilling and extracting tank

The invention discloses a multifunctional volatile oil distilling and extracting tank, and belongs to the field of traditional Chinese medicine extracting equipment. The multifunctional volatile oil distilling and extracting tank comprises a tank body, a tank cap, a tank bottom and a steam supply system, and the tank cap is connected with an oil outlet pipe. The multifunctional volatile oil distilling and extracting tank is characterized in that the tank body is in the shape of a big-end-up cone, the tank body and the tank bottom adopt interlayers, steam is pumped into the interlayers, multiple layers of detachable separation plates are arranged in the tank body, and through holes are formed in the separation plates. The multifunctional volatile oil distilling and extracting tank can be used for extracting general medicinal oil and essential oil according to the routine and normal pressure, extracting high-boiling-point medicinal oil and essential oil containing aldehydes and alcohols at high temperature and high pressure, extracting medicinal oil and essential oil which are prone to volatilizing andloseand contain more alkenes in a vacuum decompression mode and extracting extracts, one tank has multiple purposes, distilling can be completed for one time, the equipment cost is saved, and the yield of the materials, especially volatile oil, is improved.
Owner:湖南时代阳光药业股份有限公司

Distilling production method for sandalwood essential oil and equipment

The invention discloses a distilling production method for sandalwood essential oil.The method comprises the specific steps that 1, a sandalwood plant raw material is smashed into fragments with the thickness of 1 millimeter to 6 millimeters, and the fragments are placed in a distilling cabinet; 2, steam generated by a steam boiler is led into the distilling cabinet, and the sandalwood fragments are distilled; 3, tail gas of the steam boiler is processed through a first-level dust remover and a second-level dust remover before being discharged out of a chimney; 4, the steam discharged from the distilling cabinet passes through a first-level condenser and a second-level condenser before entering a receiving tank and an excessive receiving tank, and distillate is obtained; 5, the pressure in the receiving tank is kept between 0.01 Mpa and 0.3 Mpa; 6, the distillate in the excessive receiving tank passes through a third-level condenser before being discharged into a fractionation barrel; 7, the distillate is discharged out of an essential oil outlet of the fractionation barrel, and then the sandalwood essential oil is obtained.The method is simple, the oil is discharged quickly, time is short, the obtained sandalwood essential oil is high in quality, and adopted equipment is easy to operate.
Owner:GUANGXI GUIGANG HONGLI BIOENERGY TECH CO LTD

Preparation method of whitening and moisturizing essence for dry skin

The invention discloses a preparation method of whitening and moisturizing essence for dry skin. The method is characterized in that a gas collecting ring sleeve is welded to the position, at the topend of the outer side of a raw material box, of the top end of the interior of a heating box, gas inlet holes are formed in one end of the bottom face of the gas collecting ring sleeve, gas inlet pipes are evenly welded to the top end of the interior of the raw material box, one ends of the gas inlet pipes are located in the gas inlet holes, gas blowing holes are formed in one sides of top ends ofthe gas inlet pipes, and gas outlet holes are formed in one sides of bottom ends of the gas inlet pipes. Compared with the prior art, through the use of the gas outlet holes, driving paddles, rotating columns and stirring blades, a double-layer two-way stirring effect can be achieved, the purpose of uniformly dispersing raw materials is achieved, the time required by distillation is effectively shortened, and the distillation efficiency is improved; through windproof plates and limiting plates, the temperature of gas outlets of the raw material box can be kept, and the situation that steam iscondensed in advance is effectively avoided; and driving of electric appliance elements is not needed, noise brought by the electric appliance elements is lowered, and the environmental pollution isreduced.
Owner:广州中尚生物科技有限公司

Lifting-dismounting type fire-heating ceiling pot winemaking device

The invention discloses a lifting-dismounting type fire-heating ceiling pot winemaking device which is used for solving the defects, namely great energy consumption, easiness for stream escaping, a small condensing area of the ceiling pot, insufficient cooling, much wine volatilization due to a high wine temperature, high cost, low yield, great labor strength and easiness for burning, in the background technology. The lifting-dismounting type fire-heating ceiling pot winemaking device is characterized in that five heating tubes, which are parallel to one another, at the upper end of a furnace hearth 7 are communicated with a W-shaped pot bottom; eight fire exhausting tubes 4 are arranged at the topmost end of the furnace hearth 7 above the five heating tubes 5 which are parallel to one another; cavities are internally formed in an upper ceiling pot body 15 and a lower ceiling pot body 14, and are filled with circulating cooling water; the two ends of each of five water tubes 11 are communicated with the upper ceiling pot body 15 and the lower ceiling pot body 14 respectively; a coiler secondary condenser is composed of a spiral coiled tube 12 and a condensing barrel 3. The lifting-dismounting type fire-heating ceiling pot winemaking device has the advantages of being energy-saving and environment-friendly, great in heating area, short in distillation time, great in cooling area, time-saving and labor-saving, complete in distillation, low in cost, high in yield, safe and reliable in pressure-free operation, less in possibility of pot burning, low in distillation temperature, low in wine temperature, high in flavor substance content of a finished product wine, good in quality and good in mouthfeel. The lifting-dismounting type fire-heating ceiling pot winemaking device is used for making wine.
Owner:周取闻

Method for recycling dimethyl sulfoxide from explosive-containing dimethyl sulfoxide waste liquid

The invention discloses a method for recycling dimethyl sulfoxide (DMSO) from explosive-containing dimethyl sulfoxide waste liquid. The method comprises the following steps: adding the waste liquid into a distillation flask; refluxing in condensed water, in vacuum and in an oil bath, wherein the refluxing temperature is 50 DEG C to 52 DEG C at the beginning; improving a heating temperature and refluxing under the conditions that the temperature of the oil bath is 86 DEG C to 90 DEG C and the vacuum degree is 0.088MPa; after no refluxing liquid exists, adding the waste liquid without water into a rectification bottle; refluxing by a system under the conditions of condensed water, vacuum and oil bath, wherein the refluxing temperature is 95 DEG C to 97 DEG C; after refluxing for a period of time, stopping heating when the volume of a residual solution is reduced to be 1/3 to 1/5 of the volume of a stock solution; condensing and recycling to obtain liquid, namely the dimethyl sulfoxide. By adopting a method combining decompression and distillation and decompression and rectification, the disadvantage of high energy consumption of an existing method for recycling the dimethyl sulfoxide is avoided; distilled water is discharged when reaching the standards; the purity of the rectified DMSO reaches index requirements and can be used for recrystallizing explosive octogen.
Owner:INST OF CHEM MATERIAL CHINA ACADEMY OF ENG PHYSICS

Method for continuously distilling aromatic oil by subsectional temperature control

The invention relates to a method for continuously distilling aromatic oil by subsectional temperature control. The method is characterized by comprising the following steps of: after cutting raw materials to crushed aggregates, falling to a mobile conveying device; and forming a close and independent distilling work station by different distilling area and corresponding steam areas; continuously passing through the crushed aggregates by all distilling work stations to complete distillation step by step. The method provided by the invention has the positive effects that the daily handling capacity is improved by continuous feeding, distillation and discharge. Through closed cutting, vapor-solid materials are more uniformly contacted, so that vapor collapse and short circuit are effectively avoided. The temperature is controlled by sub-sections and is gradually raised to the benefit of more adequate distillation-off of aromatic oil (conventional components) in raw materials; different azeotropes (coarse distilling materials) which are collected in sub-sections are overcome for the convenience of post-process. Higher temperature distillation is realized. Shallow distillation overcomes the deficiency that steam is hard to penetrate through material layer during distillation in a barrel, so that the thermal efficiency of distillation is improved.
Owner:YIBIN UNIV

A method for recovering dimethyl sulfoxide from waste liquid containing explosive dimethyl sulfoxide

The invention discloses a method for recycling dimethyl sulfoxide (DMSO) from explosive-containing dimethyl sulfoxide waste liquid. The method comprises the following steps: adding the waste liquid into a distillation flask; refluxing in condensed water, in vacuum and in an oil bath, wherein the refluxing temperature is 50 DEG C to 52 DEG C at the beginning; improving a heating temperature and refluxing under the conditions that the temperature of the oil bath is 86 DEG C to 90 DEG C and the vacuum degree is 0.088MPa; after no refluxing liquid exists, adding the waste liquid without water into a rectification bottle; refluxing by a system under the conditions of condensed water, vacuum and oil bath, wherein the refluxing temperature is 95 DEG C to 97 DEG C; after refluxing for a period of time, stopping heating when the volume of a residual solution is reduced to be 1 / 3 to 1 / 5 of the volume of a stock solution; condensing and recycling to obtain liquid, namely the dimethyl sulfoxide. By adopting a method combining decompression and distillation and decompression and rectification, the disadvantage of high energy consumption of an existing method for recycling the dimethyl sulfoxide is avoided; distilled water is discharged when reaching the standards; the purity of the rectified DMSO reaches index requirements and can be used for recrystallizing explosive octogen.
Owner:INST OF CHEM MATERIAL CHINA ACADEMY OF ENG PHYSICS

A double-tower continuous feeding rectification system and control method

The present invention provides a control method and system for rectification with continuous feeding of double towers, including: feeding control, initial distillation process control, material delivery control and fine rectification process control; controlling the pressure P of 1# rectification tower 1 and pressure difference ΔP 1 , heat up until the top temperature reaches T 1 , open the control valve of the outlet outlet at the top of the tower, and wait for the rate of temperature increase at the top of the 1# rectification tower to be ΔT 1 , the initial distillation process is completed; the fine distillation process is: control the pressure difference ΔP at the top of the 2# rectification tower tower 2, Slowly increase the temperature of the tower kettle and control the heating rate ΔT 2 , control the temperature of the tower kettle at T 2 , when the top temperature reaches T 3 , to complete the fine distillation process control. The control method of the present invention adopts four continuous control steps, which ensures the continuous, safe and efficient feeding process, and improves the separation and purification efficiency of the rectification system. The invention also provides a double-tower continuous feeding rectification system, which has a reasonable raw material batching system, high rectification efficiency and high product purity.
Owner:TIANE CHEM FIBER GROUP CORP BAODING +1

High-purity dimethyl ester batch rectification device

The invention discloses a high-purity dimethyl ester batch rectification device, and particularly relates to the technical field of distillation separation, the high-purity dimethyl ester batch rectification device comprises a rectification kettle, the top end of the rectification kettle is connected with a reaction cover, the inner wall of the rectification kettle is fixedly provided with a fixed rod, and the fixed rod is sleeved with a reciprocating swing mechanism. The reciprocating swing mechanism is driven by the servo gear motor, so that the swing blades and the ratchet plates on the swing blades swing in a reciprocating manner, dimethyl ester raw materials in the rectifying kettle can be uniformly mixed, the dimethyl ester raw materials are enabled to be more fully and thoroughly rectified in cooperation with the use of the stirring blades and the stirring paddles, the utilization rate of the rectified raw materials is increased, and the production cost is reduced. The two micro air cylinders push the upper clamping plate and the lower clamping plate to move respectively, the first rubber mat and the second rubber mat are attached to the outer wall face of the reaction cover and the outer wall face of the rectifying still, the sealing performance of the reaction cover and the rectifying still is improved, the rectifying quality is improved, and redundant hot air generated by the heating plate is conveyed into the waste heat collecting box to be recycled.
Owner:安徽弋尚纺织科技有限公司

Waste lubricating oil regeneration processing device

PendingCN113214891AImprove efficiencyStable constant temperature heatingLubricant compositionProcess engineeringOil can
The invention discloses a waste lubricating oil regeneration processing device, and relates to the technical field of lubricating oil recovery equipment. The waste lubricating oil regeneration processing device comprises a main body device, a distillation device, an acid-alkali treatment device and a filtering and shunting device, the main body device is provided with a settling tank, a temperature increasing device is arranged in the settling tank, the main body device is provided with the distillation device, a treatment tank is arranged at the top of the distillation device, and a stirring device is arranged on the bottom surface of the inner wall of the distillation device. Through the settling tank and the temperature increasing device, the problem that the settling time is too long due to the fact that waste lubricating oil cannot be heated in traditional settling equipment is solved, and the problem that equipment cannot achieve full distilling due to the fact that the staying time of the waste lubricating oil in a high-temperature area is not reduced in traditional equipment is solved. Meanwhile, the filtering and shunting device is arranged, the problem that all traditional equipment needs to be stopped when filtering equipment is blocked is solved, sectional type filtering is carried out, and the problem that the filtering equipment needs to be stopped when being blocked is effectively solved.
Owner:吴文杰

Light component removal rectifying tower

The invention relates to the technical field of rectifying towers, in particular to a light component removal rectifying tower which comprises a tower body, a supporting frame, a gas phase inlet, a raw material inlet, a first filler plate, a second filler plate, a gas phase output pipe and a heating assembly, the supporting frame is fixedly connected to the outer surface of the lower end of the tower body, the position, close to the bottom end, of the outer surface of the left side of the tower body fixedly communicates with the gas phase inlet, the position, close to the upper end, of the outer surface of the right side of the tower body fixedly communicates with a raw material inlet, a first filler plate and a second filler plate are fixedly connected into the tower body, the outer surface of the upper end of the tower body is fixedly connected with a gas phase output pipe, and the heating assembly is arranged in the tower body. By arranging the heating assembly, conduction oil can circularly flow in a heating cavity I and a heating cavity II while the interior of the tower body is heated by utilizing the conduction oil, so that a liquid phase and a gas phase passing through the through holes are heated, the contact temperature of the liquid phase and the gas phase is ensured, the liquid phase and the gas phase are fully rectified, and the rectification efficiency is improved.
Owner:何金翠

Distillation device for producing chrysanthemum wine

The invention belongs to the technical field of distillation devices, and in particular relates to a distillation device for producing a chrysanthemum wine. The distillation device aims to solve the problem that the chrysanthemum is required to be distilled in the production process of the chrysanthemum wine, the existing distillation device cannot discharge slag conveniently, and the distillationeffect is general. The distillation device includes a liquid storage tank, a metal bucket is welded to the bottom end of the liquid storage tank, and the metal bucket is communicated with the liquidstorage tank. The bottom end of the metal bucket is screwed with a liquid discharge pipe, and the outer wall at the bottom end of the liquid storage tank is fixedly provided with a support frame through bolts. A steam box is hinged at the top end of the outer wall on one side of the liquid storage tank, a metal cover is welded to the top end of the steam box, and a discharge pipe is fixed to the top end of the metal cover by bolts. Metal mesh tubes equidistantly distributed are arranged on the inner wall of the steam box. According to the distillation device, the inclination angle of the steambox can be adjusted conveniently, so that materials in the metal mesh tubes can be poured conveniently, daily cleaning and maintenance are facilitated, the operation is simple, the contact area of steam and the materials can be increased, and the distillation effect is improved.
Owner:HUANGSHAN UNIV

Countercurrent distillation essential oil extraction equipment and process

The invention discloses countercurrent distillation essential oil extraction equipment and a countercurrent distillation essential oil extraction process. The essential oil extraction equipment comprises extraction tanks, a condenser and an oil-water separator which are connected in sequence; the number of the extraction tanks is at least three; each extraction tank is connected with a steam source through a steam branch pipeline; a first control valve is arranged on each steam branch pipeline; the steam outlet of each extraction tank is connected with the steam inlet of the condenser througha conveying pipeline; a second control valve is arranged on each conveying pipeline; the steam outlet of each extraction tank is connected with the steam inlet of one adjacent extraction tank througha connecting pipeline; the steam inlet of each extraction tank is connected with the steam outlet of the other adjacent extraction tank through a connecting pipeline; and third control valves are respectively arranged on the connecting pipelines between the extraction tanks which are connected in series front and back. According to the countercurrent distillation essential oil extraction equipmentand the countercurrent distillation essential oil extraction process of the invention, the extraction tanks with the multiple stages of steam inlets and outlets connected in series, heat of directlyinjected steam can be fully utilized through the extraction tanks connected in series, and the steam consumption can be saved by 50% or above.
Owner:温州阳羽机械科技有限公司

Inner barrel structure of wine-making distillation equipment

The invention discloses an inner barrel structure of wine-making distillation equipment, and belongs to the technical field of wine-making equipment. The inner barrel structure comprises a barrel body, a large rotary joint and a small rotary joint, wherein a wine taking tube assembly is arranged between the large rotary joint and the small rotary joint; the two ends of the wine taking tube assembly are separately connected and fixed with the large rotary joint and the small rotary joint, and can rotate along with the large rotary joint and the small rotary joint; the wine taking tube assembly comprises a steam conveying tube and a wine taking tube; a space is reserved between the wine taking tube and the steam conveying tube to form a steam channel; the two ends of the wine taking tube assembly are separately equipped with wine taking vertical tubes; and the wine taking tube is fixedly arranged in the steam conveying tube through the wine taking vertical tubes. According to the technical scheme adopted by the invention, the rotary steam conveying tube structure is adopted, so that the barrel body, the steam conveying tube, the wine taking vertical tubes and wine taking branch tubes rotate together; and the wine taking vertical tubes and the wine taking branch tubes are combined to realize active wine taking, so that a conventional passive wine taking mode is broken through.
Owner:贵州特征微生物研究院有限公司
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