AU2008213550B2 - Microwave rotary film concentrator - Google Patents

Microwave rotary film concentrator Download PDF

Info

Publication number
AU2008213550B2
AU2008213550B2 AU2008213550A AU2008213550A AU2008213550B2 AU 2008213550 B2 AU2008213550 B2 AU 2008213550B2 AU 2008213550 A AU2008213550 A AU 2008213550A AU 2008213550 A AU2008213550 A AU 2008213550A AU 2008213550 B2 AU2008213550 B2 AU 2008213550B2
Authority
AU
Australia
Prior art keywords
microwave
rotary evaporator
evaporator
tank
rotary
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
AU2008213550A
Other versions
AU2008213550A1 (en
Inventor
Xiaobing Sun
Haihua Wu
Wensheng Zhang
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
PHARM-TECH(TIANJIN)CO Ltd
Original Assignee
PHARM TECH TIANJIN CO Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by PHARM TECH TIANJIN CO Ltd filed Critical PHARM TECH TIANJIN CO Ltd
Publication of AU2008213550A1 publication Critical patent/AU2008213550A1/en
Application granted granted Critical
Publication of AU2008213550B2 publication Critical patent/AU2008213550B2/en
Ceased legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/0011Heating features
    • B01D1/0017Use of electrical or wave energy
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/0094Evaporating with forced circulation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/22Evaporating by bringing a thin layer of the liquid into contact with a heated surface
    • B01D1/222In rotating vessels; vessels with movable parts
    • B01D1/223In rotating vessels; vessels with movable parts containing a rotor
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B17/00Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
    • F26B17/28Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by rollers or discs with material passing over or between them, e.g. suction drum, sieve, the axis of rotation being in fixed position
    • F26B17/284Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by rollers or discs with material passing over or between them, e.g. suction drum, sieve, the axis of rotation being in fixed position the materials being dried on the non-perforated surface of heated rollers or drums
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B5/00Drying solid materials or objects by processes not involving the application of heat
    • F26B5/04Drying solid materials or objects by processes not involving the application of heat by evaporation or sublimation of moisture under reduced pressure, e.g. in a vacuum
    • F26B5/041Drying solid materials or objects by processes not involving the application of heat by evaporation or sublimation of moisture under reduced pressure, e.g. in a vacuum for drying flowable materials, e.g. suspensions, bulk goods, in a continuous operation, e.g. with locks or other air tight arrangements for charging/discharging
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B5/00Drying solid materials or objects by processes not involving the application of heat
    • F26B5/04Drying solid materials or objects by processes not involving the application of heat by evaporation or sublimation of moisture under reduced pressure, e.g. in a vacuum
    • F26B5/048Drying solid materials or objects by processes not involving the application of heat by evaporation or sublimation of moisture under reduced pressure, e.g. in a vacuum in combination with heat developed by electro-magnetic means, e.g. microwave energy

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Molecular Biology (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Constitution Of High-Frequency Heating (AREA)

Abstract

A microwave rotary film concentrator comprises an enclosed tank (1), a rotary evaporator (2), a microwave device (3), a discharge pipe for concentrated liquid (5), a condensor (6), a microwave shielding device (7), a stirring motor (8) and a vacuum system. The evaporating surface of the rotary evaporator (2) is tapered or round shaped. The angle (a) between the axis and the horizontal plane is 0 to 90˚. The rotary evaporator (2) indirectly connects to the external stirring motor (8) through a magnetic stirring device, and locates in the center of the enclosed tank (1). The enclosed tank (1) is provided with a lid which can be opened or closed. A sight glass (9) is on the lid. This invention has resolved many problems in concentration of the extracting liquid, such as slow evaporation rate, high concentration temperature, feed liquid decomposition due to be heated for a long time, unable to operate in reduced pressure as a result of intense boling of the feed liquid, low energy utilization, large dead volume, cleaning difficulty, etc. This invention has an extensive applied prospect.

Description

Microwave rotary film concentrator Field of the invention The invention relates to a concentrating device and more particularly, relates to a 5 microwave rotary film concentrator. Background of the invention Concentrating techniques are widely used in evaporation of liquid and crystallization process of composite, and these techniques include not only concentration under normal 0 pressure, concentration under reduced pressure but also include refrigerated dry. Concentration under reduced pressure is a process in which the pressure is lowered, evaporation temperature of charges is accordingly decreased, and then heat is supplied to the liquid, thus causing evaporation of the solvent and finally improving concentration and facilitating crystallization. Conventional concentration with single effect and concentration with multiple effects 5 suffer from some drawbacks such as long heating time and low heat exchange efficacy. In addition, it is easily subject to decomposition due to exposure of effective components under high temperature for a long time. Also, conventional heat exchanger includes plated structure or arrays of tubes both of which result in difficulties in cleaning surface of the exchanger and possibility of fouling, thereby leading to lowered heat transfer rate as well as significant heat 20 consumption. Moreover, possibly it will result in bumping during evaporating process, as there exist a great number of bubbles, and this always causes loss of liquid material. To obtain more effective concentration, it is necessary to decrease degree of vacuum. This decrease however, further slows down the speed of concentration and causes more component loss. The evaporation speed is proportional largely to evaporation surface area, and accordingly 25 the evaporation speed will be increased if the surface area is increased effectively. Furthermore, it is necessary at present to effectively avoid bubbling during solution evaporation process and reduce loss of effective components. 30 Summary of the invention One object of the invention is to provide a microwave rotary film concentrator which is highly effective yet causes less loss. It is an alternative object of the present invention to provide a microwave rotary film 5 concentrator which ameliorates, at least in part, at least one of the disadvantages of the prior art. The present invention provides a microwave rotary film concentrator comprises a hermetical tank, a rotary evaporator, a plurality of microwave devices, a solution feeding tube, a discharging tube for concentrated solution, a condenser, a plurality of microwave shielding devices, a stirring motor and a vacuum system, wherein the hermetical tank forms 0 major part of said microwave rotary film concentrator, and the microwave devices are provided at the inner wall of the hermetical tank; an opening connected with the condenser being located on the body of tank, and the condenser is communicated with the vacuum system via a duct; the rotary evaporator is disposed inside the tank at its center location; an evaporating surface of the rotary evaporator having a conical shape, the rotary evaporator 5 having a concentrator baffle mounted on an edge of said evaporating surface, and an angle between said evaporating surface and the baffle is between 5* and 1750; wherein an opening towards the discharging tube is defined at a location where the evaporator and the baffle are combined together; wherein the discharging tube is tangential to an inner surface of the evaporator; wherein the evaporator is coupled to a stirring motor by direct manner or 20 indirect manner; and wherein the microwave shielding devices are mounted on respective external ducts. The evaporating surface of the rotary evaporator can have a conic shape with a cone angle b is no less than 50 and smaller than 1800; and the angle between an axis of the rotary evaporator and a horizontal plane is between 0 and 90*. 25 The evaporating surface of the rotary evaporator can have a conic shape with a cone angle b between 60' and 1200; and an angle between an axis of the rotary evaporator and a horizontal plane can be between 20' and 600. The rotary evaporator can be hollow; and the evaporating surface contacting the solution is made of stainless steel or ceramic or combination thereof; wherein the the rotary 30 evaporator is filled with one or more of silicone oil, glycerin, tetra-pod Zinc Oxide Whisker 2 composite, calcined mixture of ferroferrite and polite (with a mixture ratio of 30:70); and wherein a material of the rotary evaporator can be selected from any one or more of stainless steel, quartz glass, ceramic, PTFE and plastic. The rotary evaporator can be connected indirectly with an external stirring motor through a 5 magnetic stirring device and centrally located inside the hermetical tank. The hermetical tank can have an openable lid, and a sight glass can be disposed on the lid. An angle d between a collection opening of the discharging tube of the rotary evaporator and the vertical can be between 6 0 *and 1200. The hermetical tank forms major part of the microwave rotary film concentrator, and the 0 tank has a cylindrical chamber with an openable lid provided thereon. A sight glass is disposed on the lid for checking boiling state of liquid contained in the concentrator, hence being able to adjust parameters of the concentrator. The microwave shielding device is located on the internal surface of a viewing window. One or more such as two microwave devices are placed on the inner wall of hermetical tank. An opening connected with the condenser is placed in the tank, 5 and the condenser is communicated with the vacuum system via a duct. A rotary film concentrator is set up inside the tank at its center location. The evaporating surface of the evaporator is designed to have a conic or circle shape with a cone angle b of 5-180 degree, and preferably 60-120 degree. The angle between an axis of the evaporator and horizontal plane is 0-90 degree, and more preferably is 20-60 degree. The evaporator may be either solid or 20 hollow. In case of solid evaporator, materials used to construct the evaporator include but is not limited to stainless steel, quartz glass, ceramic, PTFE (Poly-tetra-fluoro-ethene), plastic and so on. While in case of hollow evaporator, materials contacting the evaporating surface of the solution contain but is not limited to stainless steel, ceramic; the filed materials of hollow jacket comprise but is not limited to silicone oil, glycerin, tetra-pod Zinc Oxide Whisker composite, 25 calcined mixture of ferroferrite and iolite with ratio of 30:70 and the like, all these materials bringing good thermal stability and function of preventing vaporization of liquid or solid. Materials forming external layer of a jacket include but is not limited to quartz glass, ceramic, PTFE, plastic or the like, all these materials containing particles which are microwave-permeable, no microwave energy absorbable, highly heat resistive yet with low heat 30 expansion coefficient. Ceramic used to constitute the external layer of the jacket may include 3 alumina, magnesium fluoride and zinc sulfide and the like. Plastic used to constitute the external layer of the jacket may include PE (Polyethylene), PS (Polystyrene) and so on. The external edge of the conical surface of the evaporator has an annular baffle (10) mounted thereon to prevent leakage of liquid out of the evaporator. The angle c between the baffle and 5 conical surface is 5-175 degree, and preferably is 60-120 degree. A groove with semi-circle shaped section and a diameter of 0.5-2cm is formed between the baffle and conical evaporating surface. The evaporator is coupled at its bottom with the stirring motor directly or indirectly. In case of indirect connection, a magnetic stirring device is employed to connect to a magnetic 0 stirring motor located outside of the hermetical tank. While in case of direct connection, a shaft is used to connect to an external stirring motor. A liquid delivery system includes a solution feeding tube, a discharging tube for concentrated solution and corresponding pumps and ducts. An opening towards the discharging tube is defined at a location where the evaporator cone and the baffle are combined together. An angle d of 0-180 degree, preferably 60-120 degree is 5 formed between the opening and the line through the center and vertex of the circle. The distance between the tube opening and evaporating surface is 2-20mm. The discharging tube is tangential to internal surface of the cone and is opposite to rotation direction of the evaporator. A rectangular baffle (11) is disposed at a location 2-20mm far away from a collection tube opening for prevention of liquid leakage. A circular baffle (12) with a diameter of 5-8cm is 20 additionally placed at a location where a vertical line from the uppermost point of the external edge of the evaporator intersections the discharging tube. An inlet of the solution feeding tube parallel to the cone axis is located inside the evaporator and at the center thereof. A rectangular baffle (13) is located at a location which is 0.2-1cm distanced from the inlet of the solution feeding tube. The rectangle baffle (13) is tangential to the circle. Temperature sensors TI, T2, 25 T3 are provided to the solution feeding tube, solution discharging tube and hermetical tank respectively for easily controlling parameters. Microwave shielding devices are mounted on respective external ducts to shield irradiation. The invention overcomes or ameliorates at least in part, at least one of the drawbacks existing in prior art as low evaporating speed, high operation temperature, decomposition of 4 solution due to long time heating as well as difficulties in working under reduced pressure due to bumping of the solution, low energy use efficiency, large size of the equipment and difficulties in cleaning, and thus has a wide prospect of application. 5 Description of the drawings Fig. I shows a side elevation view of an embodiment of the invention; and Fig. 2 shows a front view of the embodiment of the invention. Preferred embodiments of the invention 0 The invention is described below in great detail with reference to some embodiments which are only illustrative but not intended to limit the invention. Embodiment 1 The microwave rotary film concentrator includes a hermetical tank (1), a rotary evaporator (2), a plurality of microwave generators (3), solution feeding tube (4), a discharging 5 tube for concentrated solution (5), a condenser (6), a plurality of microwave shielding device (7), a stirring motor (8) and a vacuum system. The hermetical tank forms major part of the microwave rotary film concentrator, and the tank has a cylindrical chamber with an openable lid provided thereon. A sight glass is disposed on the lid. A microwave shielding device is located on the internal surface of a viewing 20 window. One microwave device is located on the inner wall of the hermetical tank. An opening connected with the condenser is defined in the tank, and the condenser is communicated with the vacuum system via a duct. A rotary film concentrating device is disposed inside the tank at its center location. The evaporating surface of the evaporator is designed to have a conic shape with a cone angle b of 180 degree. The angle a between an axis of the evaporator and horizontal 25 plane is 90 degree. The evaporator is solid and made of stainless steel. The external edge of the conical surface of the evaporator has an annular baffle (10) mounted thereon. The angle c between the baffle and conical surface is 60 degree. A groove with semi-circle shaped section and a diameter of 2cm is formed between the baffle and conical evaporating surface. The evaporator is coupled at its bottom indirectly by a magnetic stirring device to a magnetic 30 stirring motor located outside of the hermetical tank. A liquid delivery system includes a 5 solution feeding tube, a concentrated solution discharging tube and corresponding pumps and ducts, an opening of the discharging tube located at a location where the evaporator cone and the baffle are combined together, wherein, an angle d of 120 degree is formed between the opening and the line through the center and vertex of the circle, and the distance between the 5 tube opening and evaporating surface is 0.2m. The discharging tube is tangential to internal surface of the cone and is opposite to rotation direction of the evaporator. A rectangular baffle (11) is disposed at a location 0.2m far away from a collection tube opening. A circular baffle (12) with a diameter of 8cm is additionally placed at a location where a vertical line from the uppermost point of the external edge of the evaporator intersections the discharging tube. An o inlet of the solution feeding tube parallel to the cone axis is located inside the evaporator and at the center thereof. A rectangular baffle (13) whose long plane is tangential to the circle, is located at a location which is 0.2cm distanced from the inlet of the solution feeding tube. Temperature sensors TI, T2, T3 are provided inside of the solution feeding tube, solution discharging tube and hermetical tank respectively. Microwave shielding devices are mounted 5 on respective external ducts. Embodiment 2 The microwave rotary film concentrator includes a hermetical tank (1), a rotary evaporator (2), a plurality of microwave generators (3), solution feeding tube (4), a concentrated solution discharging tube (5), a condenser (6), a microwave shielding device (7), a stirring motor (8) and 20 a vacuum system. The hermetical tank forms major part of the microwave rotary film concentrator, and the tank is a cylindrical chamber with an openable lid provided thereon. A sight glass is disposed on the lid. A microwave shielding device is located on the internal surface of a viewing window of the sight glass. Two microwave devices are located on the inner wall of the hermetical tank. 25 An opening connected with the condenser is defined in the tank, and the condenser is communicated with the vacuum system via duct. A rotary film concentrating device is disposed inside the tank at its center location. The evaporating surface of the evaporator is designed to have a conic shape with a cone angle b of 60 degree. The angle a between an axis of the evaporator and horizontal plane is 0 degree. The evaporator is hollow and made of stainless 6 steel. The hollow jacket is filled with tetra-pod Zinc Oxide Whisker composite, while the outer layer of the jacket is sealed with ceramic. The external edge of the conical surface of the evaporator has an annular baffle (10) mounted thereon, and the angle c between the baffle and conical surface is 120 degree. A groove with semi-circle shaped section and a diameter of 5 0.5cm is formed between the baffle and conical evaporating surface. The evaporator is coupled at its bottom indirectly by a magnetic stirring device to a magnetic stirring motor located outside of the hermetical tank. A liquid delivery system includes a solution feeding tube, a discharging tube for concentrated solution and corresponding pumps and ducts. An opening towards the discharging tube is defined at a location where the evaporator cone and the baffle 0 are combined together. An angle d of 180 degree is formed between the opening and the line through the center and vertex of circle. The distance between the tube opening and evaporating surface is 2cm. The discharging tube is tangential to internal surface of the cone and is opposite to rotation direction of the evaporator. A rectangular baffle (11) is disposed at a location lcm far away from a collection tube opening. A circular baffle (12) with a diameter of 5cm is 5 additionally placed at a location where a vertical line from the uppermost point of the external edge of the evaporator intersections the discharging tube. An inlet of the solution feeding tube parallel to the cone axis is located inside the evaporator and at the center thereof. A rectangular baffle (13) whose long plane is tangential to the circle, is located at a location which is 2cm distanced from the inlet of the solution feeding tube. Temperature sensors Tl, T2, T3 are 20 provided to the solution feeding tube, solution discharging tube and hermetical tank respectively for easily controlling parameters. Microwave shielding devices (7) are mounted in respective external ducts. Embodiment 3 The microwave rotary film concentrator includes a heretical tank (1), a rotary evaporator 25 (2), a plurality of microwave generators (3), solution feeding tube (4), a discharging tube for concentrated solution (5), a condenser (6), a plurality of microwave shielding device (7), a stirring motor (8) and a vacuum system. The hermetical tank forms major part of the microwave rotary film concentrator, and the tank has a cylindrical chamber with an openable lid provided thereon. Two sight glasses are 7 disposed on the lid. There is a microwave shielding device located on the internal surface of a viewing window of the sight glass. One microwave device is fixed inside the solution feeding tube which locates outside of the hermetical tank. There is an opening connected with the condenser in the tank, and the condenser is communicated with the vacuum system via a duct. 5 A rotary film concentrating device is disposed inside the tank at its center location. The evaporating surface of the evaporator is designed to have a conic shape with a cone angle b of 120 degree. The angle a between an axis of the evaporator and horizontal plane is 30 degree. The evaporator is solid and its evaporating surface is made of PTFE (Poly-tetra-fluoro-ethene). The external edge of the conical surface of the evaporator has an annular baffle (10) mounted 0 thereon. The angle c between the baffle and conical surface is 60 degree. A groove with semi-circle shaped section and a diameter of 2cm is formed between the baffle and conical evaporating surface. The evaporator is coupled at its bottom directly by a shaft to a stirring motor located outside of the hermetical tank. A liquid delivery system includes a solution feeding tube, a concentrated solution discharging tube and corresponding pumps and ducts. An 5 opening towards the discharging tube is defined at a location where the evaporator cone and the baffle are combined together. An angle d of 60 degree is formed between the opening and the line through the center and vertex of the circle. The distance between the tube opening and evaporating surface is 0.2cm. The discharging tube is tangential to internal surface of the cone and is opposite to rotation direction of the evaporator. A rectangular baffle (11) is disposed at a 20 location 1cm far away from a collection tube opening. A circular baffle (12) with a diameter of 3cm is additionally placed at a location where a vertical line from the uppermost point of the external edge of the evaporator intersections the discharging tube. An inlet of the solution feeding tube parallel to the cone axis is located inside the evaporator and at the center thereof. A rectangular baffle (13) whose long plane is tangential to the circle, is located at a location 25 which is 1cm distanced from the inlet of the solution feeding tube. Temperature sensors Tl, T2, T3 are provided to the solution feeding tube, solution discharging tube and hermetical tank respectively for easily controlling parameters. Microwave shielding devices (7) are mounted on respective external ducts. 8 The condenser is coupled with the tank through a duct. The condenser is of a general type (which includes arrays of tubular structure or plated structure, but in practice the latter is employed often), as shown in Fig. 1. In the figure, symbol ( 21 ) denotes inlet for cooled water, ( 24 ) denotes outlet for cooled water, ( 22 ) indicates an external vacuum system, and ( 23 ) 5 represents an outlet for coolant which is cooled with steam lysosome by a cooler, and the discharged liquid enters into a storage tank for collection. Symbol (25) represents connection to a diluted solution tank, while (26) represents a tank for containing concentrated solution. The microwave rotary film concentrator of the invention obtains several effects. For example, by way of microwave heating, problems such as low efficiency of stream heating and 0 large size are eliminated, thus effectively causing reduction in size of the concentrator. By way of rotation, the liquid is forced to become film by centrifugal forces, thus effectively leading to increase in evaporating area, reducing heating duration, and improving stability of the substance. This is suitable to concentrate substance which is sensible to heat. At the same time, bubbling of the substance is also prohibited in an effective manner under centrifugal force, and 5 as a result, the applicability of the concentrator is further extended. Using magnetic stirring device as the drive device of the rotary evaporator, problems such as leakage of lubricant oil and destruction of vacuum due to bad sealing quality existed in conventional shaft transmission are overcome. Moreover, the evaporator with smooth surface can be monitored directly. The entire equipment can be disassembled, and therefore can be cleaned completely, thereby 20 avoiding pollution. By way of microwave heating, fouling which would otherwise accumulated by steam heating and which would result in low thermal efficiency, is prevented, thus preventing the increase in energy consumption. 9

Claims (9)

1. A microwave rotary film concentrator comprises a hermetical tank, a rotary evaporator, a plurality of microwave devices, a solution feeding tube, a discharging tube for concentrated solution, a condenser, a plurality of microwave shielding devices, a stirring motor and a vacuum system, wherein the hermetical tank forms major part of said microwave rotary film concentrator, and the microwave devices are provided at the inner wall of the hermetical tank; an opening connected with the condenser being located on the body of tank, and the condenser is communicated with the vacuum system via a duct; the rotary evaporator is disposed inside the tank at its center location; an evaporating surface of the rotary evaporator having a conical shape, the rotary evaporator having a concentrator baffle mounted on an edge of said evaporating surface, and an angle c between said evaporating surface and the baffle is between 50 and 1750; wherein an opening towards the discharging tube is defined at a location where the evaporator and the baffle are combined together; wherein the discharging tube is tangential to an inner surface of the evaporator; wherein the evaporator is coupled to a stirring motor by direct manner or indirect manner; and wherein the microwave shielding devices are mounted on respective external ducts.
2. The microwave rotary film concentrator according to claim 1, wherein the evaporating surface of the rotary evaporator is designed to have a conic shape with a cone angle b is no less than 50 and smaller than 1800; and the angle between an axis of the rotary evaporator and a horizontal plane is between 0 and 90'.
3. The microwave rotary film concentrator according to claim 1, wherein the evaporating surface of the rotary evaporator is designed to have a conic shape with a cone angle b between 60' and 1200; and an angle between an axis of the rotary evaporator and a horizontal plane is between 20* and 60'. 10
4. The microwave rotary film concentrator according to claim 2 or 3, wherein the rotary evaporator is hollow; and the evaporating surface contacting the solution is made of stainless steel or ceramic or combination thereof; wherein the the rotary evaporator is filled with one or more of silicone oil, glycerin, tetra-pod Zinc Oxide Whisker composite, calcined mixture of ferroferrite and iolite (with a mixture ratio of 30:70); and wherein a material of the rotary evaporator is selected from any one or more of stainless steel, quartz glass, ceramic, PTFE and plastic.
5. The microwave rotary film concentrator according to any one of claims Ito 3, wherein the rotary evaporator is connected indirectly with an external stirring motor through a magnetic stirring device and centrally located inside the hermetical tank.
6. The microwave rotary film concentrator according to any one of claims 1 to 3, wherein the hermetical tank has an openable lid, and a sight glass is disposed on the lid.
7. The microwave rotary film concentrator according to any one of claims Ito 3, wherein an angle d between a collection opening of the discharging tube of the rotary evaporator and the vertical is between 6 0 'and 1200.
8.The microwave rotary film concentrator according to claim 1, wherein the evaporating surface of the rotary evaporator has a conic shape with a cone angle b of between 600 and 1200; an angle a between an axis of the rotary evaporator and the horizontal plane being between 200 and 600; the rotary evaporator having a concentrator baffle mounted on the edge of its conical evaporating surface, and the angle c between the conical evaporating surface and the baffle being between 60 and 1200; an angle d between an collection tube of the discharging tube of the rotary evaporator and the vertical being between 600 and 1200; the rotary evaporator being connected indirectly with an external stirring motor through a magnetic stirring device and centrally located inside the hermetical tank; the hermetical tank has an openable lid provided thereon, and a sight glass is disposed on the lid. 11
9. A microwave rotary film concentrator as herein described with reference to Figures 1 and 2 of the accompanying drawings. 12
AU2008213550A 2007-02-01 2008-01-10 Microwave rotary film concentrator Ceased AU2008213550B2 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
CN2007100566921A CN101234257B (en) 2007-02-01 2007-02-01 Microwave rotating thin film concentrator
CN200710056692.1 2007-02-01
PCT/CN2008/070067 WO2008095422A1 (en) 2007-02-01 2008-01-10 Microwave rotary film concentrator

Publications (2)

Publication Number Publication Date
AU2008213550A1 AU2008213550A1 (en) 2008-08-14
AU2008213550B2 true AU2008213550B2 (en) 2011-09-15

Family

ID=39681272

Family Applications (1)

Application Number Title Priority Date Filing Date
AU2008213550A Ceased AU2008213550B2 (en) 2007-02-01 2008-01-10 Microwave rotary film concentrator

Country Status (5)

Country Link
JP (1) JP2010517738A (en)
CN (1) CN101234257B (en)
AU (1) AU2008213550B2 (en)
DE (1) DE112008000296T5 (en)
WO (1) WO2008095422A1 (en)

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2578975A1 (en) 2011-10-05 2013-04-10 Sanofi Pasteur Sa Rotary drum freeze-dryer
EP2578974A1 (en) 2011-10-05 2013-04-10 Sanofi Pasteur Sa Process line for the production of freeze-dried particles
UA111631C2 (en) 2011-10-06 2016-05-25 Санофі Пастер Са HEATING DEVICE FOR ROTOR DRUM LYOPHILE DRYER
EP2578976A1 (en) 2011-10-06 2013-04-10 Sanofi Pasteur Sa Rotary drum for use in a vacuum freeze-dryer
CN102878783A (en) * 2012-10-09 2013-01-16 边浩光 Continuous drying machine
CN105879417A (en) * 2014-12-23 2016-08-24 江南大学 Method for removing moisture in recycled silicon wafer cutting fluid through thin-layer multi-turn-surface evaporator
CN104857734B (en) * 2015-04-29 2017-08-25 昆明理工大学 A kind of microwave evaporation device, using and application process
US10632396B2 (en) * 2015-04-29 2020-04-28 Kunming University Of Science And Technology Microwave flash evaporation process and apparatus and use thereof
CN105222179B (en) * 2015-10-09 2017-07-04 广东美的厨房电器制造有限公司 Micro-wave oven
CN107869897A (en) * 2017-10-25 2018-04-03 长沙科悦企业管理咨询有限公司 Medicinal material cleaning, drying integrated device
KR102224126B1 (en) * 2018-04-05 2021-03-08 주식회사 세븐킹에너지 Synthesis Process of Ceramic Solid Electrolyte for Lithium Secondary Batteries
CN115818904B (en) * 2023-02-14 2023-04-21 四川省生态环境科学研究院 Industrial high-salt wastewater treatment method

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5229010A (en) * 1991-07-01 1993-07-20 Progressive Recovery, Inc. Rotating microwave contaminated materials treating apparatus and method of using thereof
CN1436997A (en) * 2002-02-09 2003-08-20 中国科学院过程工程研究所 Rotary continuous microwave drier

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4057907A (en) * 1974-07-18 1977-11-15 Rapino Norman G Method and apparatus for drying clothes
JPS614501A (en) * 1984-06-15 1986-01-10 Ulvac Corp Microwave-heating centrifugal evaporator
JPS63133493A (en) * 1986-11-22 1988-06-06 株式会社 サンクル Container which absorbs microwave and generates heat
JPH061718B2 (en) * 1989-02-17 1994-01-05 松下電器産業株式会社 Electromagnetic energy conversion heating material
JP2541655B2 (en) * 1989-03-31 1996-10-09 住友電気工業株式会社 Cooker for microwave oven
JPH0445885A (en) * 1990-06-08 1992-02-14 Konica Corp Method and apparatus for treating used processing solution for non-silver salt photosensitive material
JPH0467819A (en) * 1990-07-06 1992-03-03 Koubeya:Kk Cooking container for microwave oven
JP2590568Y2 (en) * 1992-09-18 1999-02-17 株式会社大川原製作所 Structure for preventing scattering of raw material liquid in thin film vacuum evaporator
DE4319498A1 (en) * 1993-04-29 1994-11-03 Werner Lautenschlaeger Rotary evaporator
JP4349943B2 (en) * 2004-03-18 2009-10-21 株式会社大慶 rice cooker
CN2858020Y (en) * 2005-09-16 2007-01-17 周森安 Horizontal internal rotation thin-film evaporator
CN201026400Y (en) * 2007-02-01 2008-02-27 发泰(天津)科技有限公司 Microwave rotating film concentrator

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5229010A (en) * 1991-07-01 1993-07-20 Progressive Recovery, Inc. Rotating microwave contaminated materials treating apparatus and method of using thereof
CN1436997A (en) * 2002-02-09 2003-08-20 中国科学院过程工程研究所 Rotary continuous microwave drier

Also Published As

Publication number Publication date
CN101234257A (en) 2008-08-06
AU2008213550A1 (en) 2008-08-14
WO2008095422A1 (en) 2008-08-14
CN101234257B (en) 2011-07-27
JP2010517738A (en) 2010-05-27
DE112008000296T5 (en) 2010-05-12

Similar Documents

Publication Publication Date Title
AU2008213550B2 (en) Microwave rotary film concentrator
CN201482226U (en) Glass lining high-efficiency rotating scraping plate film evaporator
CN205182210U (en) Centrifugation of multilayer disk type and gravity film forming microwave evaporation plant
CN212914605U (en) High-efficient evaporation crystallization device
CN112245947A (en) Single-effect external circulation concentrator based on condensation bead collecting mechanism
CN105251225B (en) A kind of multilayer disc-stack centrifuge and gravity film forming microwave evaporation device
CN211069048U (en) A evaporation cauldron for producing industry aluminum sulfate
CN105819546A (en) Oil-water separating device, and oil sludge separating apparatus including same
CN201026400Y (en) Microwave rotating film concentrator
CN101693148A (en) Novel vacuum concentrator
WO2022142184A1 (en) Forced circulation evaporator for sewage treatment of fossil fuel power plant
CN205856033U (en) High-salt wastewater vacuum continuous evaporation dry integrated machine
CN205287652U (en) Horizontal scraper blade concentrator of frequency conversion
CN111298685A (en) Traditional Chinese medicine production transfer method
CN204932896U (en) Novel monotubular formula thin film evaporator
CN206504306U (en) Cyclone separating rises film pure steam generator
CN213994886U (en) Box-type falling film crystallizer
CN209722081U (en) Skeleton symbol Chinese mugwort essential oil refining equipment
CN109589627A (en) A kind of thin film evaporator
CN102091425B (en) Film flash evaporation proportion difference type concentrator
CN205391759U (en) Take two hot type high efficiency worker evaporation cauldrons that add of recovery unit
CN211486607U (en) Forced circulation evaporation crystallizer
CN105233514B (en) A kind of thin film evaporator and its application method based on separate heat pipe
CN205598674U (en) Concentrating tank
CN116768306B (en) Waste water evaporating crystallizer device

Legal Events

Date Code Title Description
FGA Letters patent sealed or granted (standard patent)
MK14 Patent ceased section 143(a) (annual fees not paid) or expired