CN2880206Y - Microwave heating concentrating apparatus - Google Patents

Microwave heating concentrating apparatus Download PDF

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Publication number
CN2880206Y
CN2880206Y CN 200620101218 CN200620101218U CN2880206Y CN 2880206 Y CN2880206 Y CN 2880206Y CN 200620101218 CN200620101218 CN 200620101218 CN 200620101218 U CN200620101218 U CN 200620101218U CN 2880206 Y CN2880206 Y CN 2880206Y
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China
Prior art keywords
microwave
heating
solvent
utility
ultrasonic
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Expired - Fee Related
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CN 200620101218
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Chinese (zh)
Inventor
贺小群
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Individual
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Individual
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Priority to CN 200620101218 priority Critical patent/CN2880206Y/en
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Publication of CN2880206Y publication Critical patent/CN2880206Y/en
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Abstract

The utility model relates to a liquid solvent evaporation concentration equipment, in particular to the microwave heating concentration plant that saves energy and pipeline valve etc facilities greatly. The utility model is characterized in that, on the basis of original heating concentration plant structure, bottom of heating chamber (5) is mounted with ultrasonic element (4); top of heating chamber (5) is mounted with microwave element (9); said ultrasonic element (4) and microwave element (9) is electrically connected with control device (10) to form overall microwave heating concentration plant. The concentration equipment has the advantages of that the microwave energy is utilized to heat solvent water mist surface, solvent water mist is generated by ultrasonic, so solvent is concentrated by evaporation, electricity saving effect is very notable, coal, boiler room, a great quantity of pipes and valves are not required, so as to save energy, reduce cost.

Description

The heating using microwave enrichment facility
Technical field
The utility model relates to liquid, solvent evaporation concentration equipment, particularly the heating using microwave enrichment facility of facility such as energy savings and pipeline valve greatly.
Background technology
Liquid in the past, solvent evaporation concentration equipment, its general structure comprises inlet, vaporization chamber, form, heating clamber, receiver, cooler, condenser and control device, additional many pipeline valves.Still formula, shell and tube, lifting membrane type respond, all be to adopt outer heating such as steam, deep fat, electricity to carry out work by the mode of tube wall transmission heat again, in order to improve the thermal efficiency, once adopt two effects, triple effect etc. to use the method for thermal source repeatedly, but all fundamentally do not solve the huge problem of power consumption.Basic heating schedule all is to enter boiler combustion with coal in the normal food chemical plant, the heating tube wall, and the feedwater of conducting heat, the water generation steam that seethes with excitement again, in the container in pipe long-distance is transported to workshop, the heating tube wall conducts heat and gives solvent.As use electric oil, though simpler than adding hot water, oily bigger as the heat transfer object expense with coal, the cost height, not as cheap water vapour, so most of producer is up to now, still adopting the burning coal to go out steam is main heating source.In and for example at present both at home and abroad all pharmaceutical factories all be pipeline in length and breadth, valve gathers, and need drop into substantial contribution when founding the factory, and also needs a lot of personnel to carry out maintaining at ordinary times.
The utility model content
The purpose of this utility model is at above-mentioned defective, and a kind of heating using microwave enrichment facility is provided.
The technical solution of the utility model is on original heating enrichment facility architecture basics, in the bottom of heating clamber (5) ultrasonic element (4) is installed, and on the top of heating clamber (5) microwave component (9) is installed; Said ultrasonic element (4), microwave component (9) are electrically connected with control device (10).Constitute new type of microwave heating enrichment facility.
The utility model has the advantages that and utilize ultrasonic atomizatio, microwave energy heated solvent water smoke surface makes the solvent evaporation and concentration, and it is very obvious to economize on electricity, and need not use coal, does not build the boiler room, does not have a large amount of pipeline valves, saves cost.
Description of drawings
Fig. 1 is the utility model structural representation.
The specific embodiment
Further describe embodiment below in conjunction with accompanying drawing.
With reference to Fig. 1,1-inlet, 2-vaporization chamber, 3-form, 4-ultrasonic element, 5-heating clamber, 6-receiver, 7-cooler, 8-condenser, 9-microwave component, 10-control device.As shown, inventive point of the present utility model is in the bottom of heating clamber (5) ultrasonic element (4) to be installed; On the top of heating clamber (5) microwave component (9) is installed, ultrasonic element (4) and microwave component (9) are electrically connected with control device (10).The using ultrasound ripple acts in the solvent can produce vibration, makes solvent normal temperature boiling (illusion), and makes the solvent surface produce globule atomizing, and the penetration capacity of microwave energy in mist vapour is relatively poor, only produce heat, therefore make up two kinds of advantages, produce brand-new heating enrichment facility on the solvent surface.Can buy on ultrasonic element and the microwave component market, control device also is a known technology.
Operation principle: package unit is worked under condition of negative pressure, solvent enters vaporization chamber (2) and enters heating clamber (5) along pipeline from inlet (1), when quantity of solvent is higher than form (3), ultrasonic element (4) is started working, the solvent atomizing that under the effect of supersonic oscillations, comes to life, at this moment start microwave component (9) device, microwave energy acts on the water smoke surface in heating clamber (5), part water smoke is heated up rapidly, almostization enters the vaporization chamber (2) of negative pressure, enter condenser (8) along bend pipe, after cooler (7) cooling, become liquid to enter receiver (6) again.Because the penetration capacity of microwave is relatively poor, the solvent below the water smoke only part receives microwave energy, and it is unhappy to heat up, so the temperature of solvent can be too not high yet, can not destroy the active ingredient in the solvent, and the energy consumption of microwave is also little, and this is with regard to energy savings greatly.In addition, need not use coal, need not build the boiler room, not have a large amount of pipeline valves, therefore, this is the major transformation that concentrator heats in China and foreign countries.From control device (10), control the oscillation intensity of ultrasonic element (4) transducing oscillator in the operating process, can make the mist almost accelerate to run too by force, be unfavorable for the heat effect of microwave component (9) to vaporization chamber (2).Microwave component (9) heating effect also will be controlled, and prevents excessive temperature, in order to avoid the active ingredient in the solvent is damaged.The mist almost of heating wafts to vaporization chamber (2), enters bend pipe and enters condenser (8) again, also has the not heated solvent of part to flow to heating clamber (5) from vaporization chamber (2) lower end again, so circulation.

Claims (1)

1, heating using microwave enrichment facility, comprise inlet (1), vaporization chamber (2), form (3), heating clamber (5), receiver (6), cooler (7), condenser (8) and control device (10), it is characterized in that ultrasonic element (4) being installed, microwave component (9) is installed on the top of heating clamber (5) in the bottom of heating clamber (5); Said ultrasonic element (4), microwave component (9) are electrically connected with control device (10).
CN 200620101218 2006-02-24 2006-02-24 Microwave heating concentrating apparatus Expired - Fee Related CN2880206Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200620101218 CN2880206Y (en) 2006-02-24 2006-02-24 Microwave heating concentrating apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200620101218 CN2880206Y (en) 2006-02-24 2006-02-24 Microwave heating concentrating apparatus

Publications (1)

Publication Number Publication Date
CN2880206Y true CN2880206Y (en) 2007-03-21

Family

ID=37880045

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 200620101218 Expired - Fee Related CN2880206Y (en) 2006-02-24 2006-02-24 Microwave heating concentrating apparatus

Country Status (1)

Country Link
CN (1) CN2880206Y (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103331025A (en) * 2013-06-18 2013-10-02 天津科技大学 Ultrasonic evaporator
CN103344038A (en) * 2013-06-14 2013-10-09 南京航空航天大学 Microwave heating compression system and method
CN109276904A (en) * 2018-10-31 2019-01-29 焦作中维特品药业股份有限公司 A kind of high-efficiency polyethylene pyrrolidones continuous rectification reboiler and washing methods

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103344038A (en) * 2013-06-14 2013-10-09 南京航空航天大学 Microwave heating compression system and method
CN103344038B (en) * 2013-06-14 2016-04-27 南京航空航天大学 Microwave heated compressibility and method
CN103331025A (en) * 2013-06-18 2013-10-02 天津科技大学 Ultrasonic evaporator
CN109276904A (en) * 2018-10-31 2019-01-29 焦作中维特品药业股份有限公司 A kind of high-efficiency polyethylene pyrrolidones continuous rectification reboiler and washing methods

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C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20070321