CN102580333A - Evaporation system for pressure reduction and film formation through vacuum rotation - Google Patents
Evaporation system for pressure reduction and film formation through vacuum rotation Download PDFInfo
- Publication number
- CN102580333A CN102580333A CN2012100329876A CN201210032987A CN102580333A CN 102580333 A CN102580333 A CN 102580333A CN 2012100329876 A CN2012100329876 A CN 2012100329876A CN 201210032987 A CN201210032987 A CN 201210032987A CN 102580333 A CN102580333 A CN 102580333A
- Authority
- CN
- China
- Prior art keywords
- vacuum
- film forming
- liquid
- tank
- evaporation
- 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.)
- Granted
Links
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/12—Molecular distillation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/06—Flash distillation
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention relates to equipment for converting liquid-phase substances into gas-phase substances. An evaporation system for pressure reduction and film formation through vacuum rotation comprises a vacuum container, wherein an annular evaporation tank with an upper opening is arranged inside the vacuum container, the side face of the evaporation tank constitutes an evaporation face, a heating device for heating the evaporation face is arranged in the vacuum container, vacuum liquid film formation structures capable of circumferentially rotating along the evaporation tank are arranged in the evaporation tank and respectively comprise blades, a concentrated liquid adsorption pipe and a combined film forming device, the blades, the concentrated liquid adsorption pipe and the combined film forming device are arranged from front to back in sequence according to a rotation direction of each vacuum liquid film forming structure, each combined film former comprises a plurality of film formation rods and a liquid distribution pipe, the film formation rods are distributed along a vertical direction and extend in a horizontal direction, and the liquid distribution pipe is used for conveying feed liquid to the film formation rods. The invention provides the evaporation system for pressure reduction and film formation through vacuum rotation, which can be used for actively controlling the formation conditions for stock liquid evaporation so as to instantly evaporate the stock liquid, and the problem of lower evaporation efficiency in a process of passively evaporating the stock liquid is solved.
Description
Technical field
The present invention relates to liquid phase substance is converted into the equipment of gaseous substance, a kind ofly reduce pressure and form liquid film and realize making the instantaneous vapo(u)rization system that puts in place that concentrates of feed liquid with the ACTIVE CONTROL that reaches evaporation conditions through rotary action thereby relate in particular to.
Background technology
Seawater is desalinated or the method that solution concentrates is had two kinds: a kind ofly be osmosis, another kind is the way of distillation.Need use evaporation equipment during the way of distillation.
The operation principle of existing evaporation equipment is for the liquefied mixture of the material that is processed (below be referred to as feed liquid) is heated, through changing the evaporation rate that methods such as temperature, surface area improve the liquid material.
Chinese patent Granted publication number for 201978517U, Granted publication day be September 21 in 2011 day, be called the vapo(u)rization system that discloses a kind of single stage type in the patent documentation of " a kind of bittern concentration and evaporation system use vaporization chamber ".The structure of the vapo(u)rization system in this patent is: comprise vacuum tank, heating chamber and the circulating pump that feed liquid is circulated between vacuum tank and heating chamber.On vacuum tank top the gas condensing means is set during use; Feed liquid is contained in the vacuum tank; Circulating pump circulates feed liquid between vacuum tank and heating chamber; Feed liquid is heated in heating chamber, and the feed liquid of heat produces Evaporation Phenomenon when getting back in the vacuum tank and forms gas, and gas becomes liquid again under the effect of gas condensing means.
Number be 2003101071932 in one Chinese patent application, open day be June 8 in 2005 day, be called in the patent documentation of " spray exchange type desalinator for seawater " and disclose another kind of single stage type evaporation equipment.Evaporation equipment in this patent comprises vaporization chamber and is positioned at the refrigerant condenser of vaporization chamber, and seawater spraying discharges heat and seawater is heated seawater produced evaporate to the refrigerant condenser in the use during refrigerant condensation in the condensation condenser.Steam flows to and is condensed into water in the condensation chamber.
The evaporation equipment of above single stage type heats feed liquid because of need external heat source always, and the heat that is discharged during condensation of gas can not get utilizing again, therefore has capacity usage ratio low (efficiency is low), problem that evaporation efficiency is low.
In order to improve evaporation efficiency and efficiency; Design multiple-effect (multistage) vapo(u)rization system, be about to many over-heat-exchangers and be connected in series, first order heat exchanger heats through external heat source; Make the feed liquid in the interchanger evaporate; The steam that evaporation is produced remakes the thermal source into next heat exchanger, and steam makes when the feed liquid in the next stage heat exchanger is heated and self temperature decline both helped the condensation of steam; Play the effect that heat energy utilizes again simultaneously, thereby reduced energy consumption and improved evaporation efficiency.The vapor (steam) temperature of considering the feed liquid evaporation and forming can descend successively; Therefore temperature does not reach the evaporating temperature of feed liquid under the atmospheric pressure, reduce pressure the successively temperature of the steam that gasification temperature that (vacuumizing) make feed liquid flows into upper level of heat exchangers at different levels is complementary.Because vacuumized the restriction of difficulty, the progression of multi-effect evaporation system can not be too many.For overcoming above-mentioned deficiency, the patent documentation that number be 2005800335343 at Chinese patent, name is called " having in the multi-effect evaporation system of chamber of horizontal plate type heat exchanger the method and apparatus that distills or evaporate salt solution or certain fluid through reheated steam " is disclosing the vapo(u)rization system that a kind of progression does not belong to restriction.This system is in feed liquid evaporation and the steam that forms gets into before the next stage heat exchanger; This is had the steam that is higher than room temperature is heated to and can makes the temperature of feed liquid in the normal pressure gasified; Thereby do not need the heat exchanging device to vacuumize, thereby make progression to design arbitrarily as required.
Existing vapo(u)rization system, no matter be single-stage or multistage version; Feed liquid all is to be evaporated or repeatedly get into heat exchanger and progressively evaporate at heating region etc. passively, the air pressure in the vaporization chamber also just passively the vaccum-pumping equipment through the outside reduce.Therefore there is the lower deficiency of evaporation efficiency in existing vapo(u)rization system.
Summary of the invention
The invention provides a kind of through ACTIVE CONTROL feed liquid evaporation formation condition so that feed liquid can instantaneous completion evaporation vacuum rotate film forming decompression evaporation system, overcome feed liquid and carried out the lower problem of evaporation efficiency in the ground evaporating course with passive mode.
Above technical problem solves through following technical proposal: a kind of vacuum is rotated film forming decompression evaporation system; Comprise vacuum tank; Be provided with the annular evaporator tank of open upper end in the said vacuum tank; The side surface of said evaporator tank constitutes evaporating surface; Said vacuum tank is provided with the heater that said evaporating surface is heated; Be provided with in the said evaporator tank and can form structure along the vacuum liquid film of the circumferential rotation of evaporator tank, said vacuum liquid film forms structure and comprises according to the vacuum liquid film and form blade, concentrate adsorption tube and the combination film forming device that the rotation direction of structure sets gradually in the past backward, and said combination film forming device comprises film forming bar that some directions of level distribution are along the vertical direction extended and feed liquid flowed to the liquid distribution pipe of film forming bar.During use, give the evaporating surface heat supply, make the temperature of evaporating surface remain on feed liquid and evaporate needed temperature through heater; The vacuum liquid film forms structure in the evaporator tank rotating process; Blade on the one hand with evaporating surface remove, make the evaporating surface non-scaling, guarantee follow-up feed liquid have cleaning evaporating surface, be convenient to the adhesion of liquid film and the transmission of heat; Steam in the vane drive evaporator tank rises simultaneously, makes steam leave evaporating surface immediately and negative pressure band higher than the vacuum in the vacuum tank of formation at the rear of blade (with the rotation direction orientation); The instant absorption of concentrate that the concentrate adsorption tube that is positioned at the blade rear will remain on the evaporating surface is walked, and can on evaporator tank especially evaporating surface, not assemble concentrate, further guarantees the cleaning of evaporating surface; When flowing out in the film forming bar of feed liquid from the combination film forming device; Because action of centrifugal force; Feed liquid forms liquid film and evaporates part on the surface of film forming bar; When the liquid film that does not evaporate is transported to the evaporating surface that is positioned at negative pressure band place, the thinner thickness of liquid film, liquid film one contact and evaporating face is promptly fallen by flash evaporation.Remain in the concentrate that is on the evaporating surface this moment, the concentrate adsorption tube that concentrate is arrived soon after in time absorption is walked.
As preferably, said blade recedes along the blade rotation direction.Blade is in the evaporator tank rotating process, and blade can play guide effect to steam, makes steam leave evaporator tank more apace, and the pressure of the vacuum area at blade rear is lower, plays the effect of further raising evaporation efficiency.
As preferably, said film forming bar is perpendicular to the sidewall of said vaporization chamber.The liquid film of transferring on the evaporating surface is thick more even, and is better to the evaporation effect of feed liquid.
As preferably, be provided with the quantitative liquid dispenser of quantitative conveying feed liquid to the said film forming bar in the said liquid distribution pipe, said film forming bar is cylindrical bar or conical rod.Through the flow of quantitative liquid dispenser ACTIVE CONTROL feed liquid, the controllability when making evaporation is better, and feed liquid is delivered in the process on the evaporating surface, can not produce and spill phenomenon, can not contain drop in the steam, and the degree of purity of steam is good; The dosing bar is actual when being conical rod, can further reduce the thickness that is delivered to the liquid film on the evaporating surface.
As preferably, said concentrate adsorption tube is positioned at the outside of said vaporization chamber, and said concentrate adsorption tube is provided with the inlet that several distribute along the vertical direction towards a side of said evaporating surface.Timely cleaning effect to the concentrate on the evaporating surface is better, and concentrate can not produce trickling and gather on evaporating surface, can keep the cleaning of evaporator tank and interior each parts thereof, and the degree of purity of steam is good.
The present invention also comprises the vacuum source that is positioned at vacuum tank; Be provided with the annular concentrate accumulator tank that circumferentially extends along vacuum tank in the said vacuum tank; The upper end of said concentrate adsorption tube links together with the import of vacuum source, and the port of export of said vacuum source is connected with concentrate is transported to the concentrate delivery pipe in the concentrate accumulator tank.Vacuum source driving adsorption tube is set concentrate is adsorbed advantages of good adsorption effect; The concentrate accumulator tank is set, and it is convenient to make when be arranged in concentrate adsorption tube that vacuum tank is kept in motion discharges concentrate.
The present invention includes and drive dosing rotating disk and the motor that said vacuum liquid film forms the structure rotation, the fluid course that said dosing rotating disk is provided with feed tube and feed tube is communicated with liquid distribution pipe, said feed tube is coaxial with said dosing rotating disk.During use, feed tube is with the butt joint of feed liquid supply pipe or charging basket, starter, and motor drives the dosing dial rotation, and the dosing rotating disk drives the vacuum liquid film and forms structure circumferentially moving along evaporator tank in evaporator tank; Feed liquid gets into liquid distribution pipe successively behind feed tube, fluid course.Be convenient to feed liquid is outputed on the combination film forming device of rotation.
As preferably, be provided with heater in the said evaporator tank.Heater can play the effect that the steam of accelerating in the evaporator tank leaves evaporator tank, and what help evaporating carries out continuously.
As preferably, said heater is positioned on the diapire or madial wall of said evaporator tank.Because the madial wall of evaporator tank is far away from evaporating surface, this place's temperature is lower, therefore selects diapire or madial wall position that steam is heated, and drives the better effects if that steam leaves evaporator tank.
As preferably, said heater comprises that being looped around said evaporator tank external heated chamber is arranged on the shower nozzle towards the evaporator tank lateral wall in the heating chamber with several.During use, hydrothermal solution or vapours (below be referred to as the thermal source medium) are run on the outer surface of lateral wall of evaporator tank through shower nozzle, realize heating evaporating surface.Effective when evaporating surface is heated.
The present invention has following advantage, through combination film forming device and evaporating surface are set, feed liquid is evaporated on evaporating surface with the form of liquid film; Passive being evaporated to initiatively that becomes feed liquid evaporated, and blade is set, and forms vacuum area in the process of blade rotation; And liquid film can evaporate in the shorter time, thereby realized flash evaporation when correspondingly on the position corresponding to vacuum area of evaporating surface, evaporating; Make the feed liquid that gets into evaporation region can once meet the requirements of enrichment stage, so evaporation efficiency is high, during with liquid film evaporation; Be difficult for producing boiling phenomenon, can not also have drop in the steam, the high purity of steam; Because the vacuum liquid film forms structure and in evaporator tank, gyrates, so under the effect of blade and concentrate adsorption tube, the heat-transfer effect when evaporating surface can keep non-scaling, evaporating surface to conduct heat to liquid film at any time is good, heat utilization ratio is high.
Description of drawings
Fig. 1 is the sketch map of the embodiment of the invention one.
Fig. 2 is A-A schematic cross-section of Fig. 1.
Fig. 3 be the concentrate adsorption tube among Fig. 1 B to enlarged diagram.
Fig. 4 is the sketch map of the embodiment of the invention two.
Among the figure: vacuum tank 1, evacuating valve 11, concentrate accumulator tank 12, concentrate vent valves 121, feed liquid bucket 2, liquor inlet valve 21; Evaporator tank 3, evaporating surface 31, the vacuum liquid film forms structure 4, blade 41, combination film forming device 42, liquid distribution pipe 421; Film forming bar 422, quantitative liquid dispenser 423, concentrate suction pipe 43, inlet 431, vacuum source 44, concentrate delivery pipe 441; Dosing rotating disk 5, feed tube 51, motor 6, heater 7, heater 8; Heating chamber 81, thermal source media outlet valve 811, shower nozzle 82, the thermal source medium gets into arm 821, thermal source medium main 83.
The specific embodiment
Below in conjunction with accompanying drawing and embodiment the present invention is further described.
Embodiment one:
Referring to Fig. 1, a kind of vacuum is rotated film forming decompression evaporation system, comprises vacuum tank 1.Vacuum tank 1 is made for stainless steel.The roof of vacuum tank 1 is provided with evacuating valve 11.The top of vacuum tank 1 is reserved with the space that the steam condensed system is installed.
The sidewall middle part of vacuum tank 1 is provided with concentrate accumulator tank 12.Concentrate accumulator tank 12 is along the circumferential extension of vacuum tank 1.Concentrate accumulator tank 12 is provided with concentrate vent valves 121.
The diapire of vacuum tank 1 is provided with and is positioned at vacuum tank 1 inner cylindrical feed liquid bucket 2.
The bottom of feed liquid bucket 2 is provided with liquor inlet valve 21.Be provided with motor 6 in the feed liquid bucket 2.The top of feed liquid bucket 2 is provided with dosing rotating disk 5.Motor 6 is used to drive dosing rotating disk 5 and rotates.Dosing rotating disk 5 is provided with the feed tube 51 that extend in the feed liquid bucket 2.
Form the annular evaporator tank 3 of open upper end between feed liquid bucket 2 and the vacuum tank 1.Evaporator tank 3 is with dosing rotating disk 5 coaxial lines.The inner surface of the lateral wall of evaporator tank 3 is that lateral surface constitutes evaporating surface 31.
Be provided with the vacuum liquid film in the evaporator tank 3 and form structure 4.The vacuum liquid film forms structure 4 and comprises blade 41, concentrate suction pipe 43 and combination film forming device 42.Blade 41 is fixed on the combination film forming device 42.The upper end of blade 41 is concordant with feed liquid bucket 2.Combination film forming device 42 comprises the film forming bar 422 on the liquid distribution pipe 421 that is connected of liquid distribution pipe 421 and some distributions along the vertical direction.Film forming bar 422 along continuous straight runs extend.Liquid distribution pipe 421 vertically extends.The upper end of liquid distribution pipe 421 is fixed on the dosing rotating disk 5.Liquid distribution pipe 421 is connected together through the fluid course that is arranged in the dosing rotating disk 5 with feed tube 51.Dosing rotating disk 5 is provided with vacuum source 44.Concentrate suction pipe 43 extends along the vertical direction.To be the port of export be docking together with the entrance point of vacuum source 44 in the upper end of concentrate suction pipe 43, in the outlet of vacuum source 44 to being connected to concentrate delivery pipe 441.
The diapire of evaporator tank 3 is provided with heater 7.Heater 7 is the loop configuration along the circumferential extension of evaporator tank 3.
Vacuum tank 1 outside is provided with heater 8.Heater 8 comprises that being looped around evaporator tank 3 external heated chambeies 81 is arranged on the shower nozzle 82 towards the evaporator tank lateral wall in the heating chamber 81 with several.The diapire of heating chamber 81 is provided with thermal source media outlet valve 811.Shower nozzle 82 is the tetrapyamid shape structure.Shower nozzle 82 is provided with the thermal source medium and gets into arm 821.The thermal source medium gets into arm 821 and passes heating chamber 81.Shower nozzle 82 vertically is divided into six rows.
Referring to Fig. 2, the vacuum liquid film forms knot enough 4 has four.Four vacuum liquid films form knot enough 4 and are symmetrically distributed in the evaporator tank 3.Evenly be arranged so that to need not counterweight the stationarity in the time of can guaranteeing to rotate.Blade 41, concentrate adsorption tube 43 and the combination film forming device 42 rotation direction C when using sets gradually in the past backward.Blade 41 in rotational direction C recedes.The width of blade 41 equates with the width of evaporator tank 3.Film forming bar 422 is a conical rod, certainly with cylindrical bar also can, film forming bar 422 is perpendicular to the sidewall of vaporization chamber 3.Be provided with quantitative liquid dispenser 423 in the liquid distribution pipe 421.Quantitatively liquid dispenser 423 is an existing product.Quantitatively liquid dispenser 423 is used for the feed liquid in the liquid distribution pipe 421 is quantitatively flowed to the surface of film forming bar 422.Concentrate adsorption tube 43 is positioned on the outside of vaporization chamber 3.Nozzle 82 among each row circumferentially evenly distributes along heating chamber 81.
In the present embodiment be all film forming bar 422 through same liquid distribution pipe 421 dosings, certainly design many liquid distribution pipes, each root liquid distribution pipe carries out dosing to the part bar in the film forming bar.In order to reduce the weight of dosing bar, easy and convenient when making rotation, can the film forming bar be designed to hollow structure.
Referring to Fig. 3, the side towards the lateral wall of vaporization chamber of concentrate adsorption tube 43 is provided with several inlets that distributes along the vertical direction 431.
During use, referring to Fig. 1, open liquor inlet valve 21, feed liquid enters in the feed liquid bucket 2 from liquor inlet valve 21.The thermal source medium thermal source medium of flowing through successively gets on arm 821 and shower nozzle 82 backs are sprayed onto evaporator tank 3 by shower nozzle 82 the lateral wall, plays the effect to evaporating surface 31 heating, and the thermal source medium of the completion heat supply that gathers in the heating chamber 81 is discharged through thermal source media outlet valve 811.External vacuum equipment vacuumizes through 11 pairs of vacuum tanks 1 of evacuating valve; Make vacuum tank 1 inside remain on vacuum state; (vacuumize is for feed liquid can be evaporated at a lower temperature; Convenient when making evaporating surface 31 maintain the evaporating temperature of feed liquid), steam and condensate system is installed in the headspace on vacuum tank 1 top.Motor 6 drives dosing rotating disk 5 and rotates, and dosing rotating disk 5 drives vacuum liquid film formation structure 4 and rotates according to the rotation direction C among Fig. 2.Feed liquid in the feed liquid bucket 2 flows in the liquid distribution pipe 421 behind feed tube 51; Quantitatively be transported on the film forming bar 422 through quantitative liquid dispenser 423 again; Because the centrifugal action of rotating; Feed liquid is dispersed on the film forming bar 422 and with membranaceous with the form of liquid film and is transported on the evaporating surface 31, and feed liquid at first produces evaporation on the surface of film forming bar 422, the liquid film played of evaporation to 31 last times of evaporating surface thinner and on evaporating surface 31, absorb heat and last flash evaporation is fallen.Under the effect of vacuum source 44, behind inlet 431, concentrate delivery pipe 441, flow in the concentrate accumulator tank 12 successively at the remaining concentrate in evaporation back on the evaporating surface at liquid film.Concentrate in the concentrate accumulator tank 12 is discharged through concentrate drain valve 121.Blade 41 can function as follows when rotating: steam is upwards driven, quickened to the steam in the evaporator tank 3 leave evaporator tank 3; Evaporating surface 31 is cleaned, help the transmission of heat; Rear at blade forms the lower vacuum area of pressure; Can shorten the evaporation time that is transported to the liquid film on the evaporating surface 31 through film forming bar 422; The low more good more contradiction of pressure when having overcome when quickening to condense the high more good more and evaporation of pressure, make evaporation with condense and can in same vacuum tank, carry out efficiently simultaneously.In the use, whether the concentration that detects concentrate meets the requirements, and (the expression evaporation effect does not reach requirement, then can improve the rotating speed of dosing rotating disk 5, reduces thickness that film forming bar 422 is transported to the liquid film on the evaporating surface 31 to improve if concentration is too low.The size of the force value of blade rear negative pressuren zone can be through changing rotating speed and controlling blade 41 and realize with the gap length between the evaporator tank 3 during evaporation.
Embodiment two, and referring to Fig. 4, with the difference of embodiment one be: evaporator tank 3 has two, and heater 8 also has two accordingly.Two evaporator tanks 3 are coaxial.In two evaporator tanks 3, all be provided with the vacuum liquid film accordingly and form structure 4 according to embodiment one described mode.Thermal source medium on all shower nozzles 82 in two heating chambers 81 gets into arm 821 and all draws through thermal source medium main 83.Feed liquid bucket 2 is arranged on the diapire outer surface of vacuum tank 1.Motor 6 is fixed on the top of vacuum tank 1.Heater 7 is positioned on the madial wall of evaporator tank 3.
Claims (10)
1. a vacuum is rotated film forming decompression evaporation system; Comprise vacuum tank; It is characterized in that; Be provided with the annular evaporator tank of open upper end in the said vacuum tank; The side surface of said evaporator tank constitutes evaporating surface, and said vacuum tank is provided with the heater that said evaporating surface is heated, and is provided with in the said evaporator tank to form structure along the vacuum liquid film of the circumferential rotation of evaporator tank; Said vacuum liquid film forms structure and comprises according to the vacuum liquid film and form blade, concentrate adsorption tube and the combination film forming device that the rotation direction of structure sets gradually in the past backward, and said combination film forming device comprises film forming bar that some directions of level distribution are along the vertical direction extended and feed liquid flowed to the liquid distribution pipe of film forming bar.
2. vacuum according to claim 1 is rotated film forming decompression evaporation system, it is characterized in that said blade recedes along the blade rotation direction.
3. vacuum according to claim 1 and 2 is rotated film forming decompression evaporation system, it is characterized in that said film forming bar is perpendicular to the sidewall of said vaporization chamber.
4. vacuum according to claim 3 is rotated film forming decompression evaporation system, it is characterized in that, is provided with the quantitative liquid dispenser of quantitative conveying feed liquid to the said film forming bar in the said liquid distribution pipe, and said film forming bar is cylindrical bar or conical rod.
5. vacuum according to claim 1 and 2 is rotated film forming decompression evaporation system; It is characterized in that; Said concentrate adsorption tube is positioned at the outside of said vaporization chamber, and said concentrate adsorption tube is provided with the inlet that several distribute along the vertical direction towards a side of said evaporating surface.
6. vacuum according to claim 5 is rotated film forming decompression evaporation system; It is characterized in that; Also comprise the vacuum source that is positioned at vacuum tank; Be provided with the annular concentrate accumulator tank that circumferentially extends along vacuum tank in the said vacuum tank, the upper end of said concentrate adsorption tube links together with the import of vacuum source, and the port of export of said vacuum source is connected with concentrate is transported to the concentrate delivery pipe in the concentrate accumulator tank.
7. vacuum according to claim 1 and 2 is rotated film forming decompression evaporation system; It is characterized in that; Comprise that driving said vacuum liquid film forms dosing rotating disk and the motor that structure is rotated; The fluid course that said dosing rotating disk is provided with feed tube and feed tube is communicated with liquid distribution pipe, said feed tube is coaxial with said dosing rotating disk.
8. vacuum according to claim 1 and 2 is rotated film forming decompression evaporation system, it is characterized in that, is provided with heater in the said evaporator tank.
9. vacuum according to claim 8 is rotated film forming decompression evaporation system, it is characterized in that said heater is positioned on the diapire or madial wall of said evaporator tank.
10. vacuum according to claim 1 and 2 is rotated film forming decompression evaporation system, it is characterized in that, said heater comprises that being looped around said evaporator tank external heated chamber is arranged on the shower nozzle towards the evaporator tank lateral wall in the heating chamber with several.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210032987.6A CN102580333B (en) | 2012-02-15 | 2012-02-15 | Evaporation system for pressure reduction and film formation through vacuum rotation |
| PCT/CN2013/070405 WO2013120403A1 (en) | 2012-02-15 | 2013-01-14 | Vacuum rotation film-forming and depressurizing evaporation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210032987.6A CN102580333B (en) | 2012-02-15 | 2012-02-15 | Evaporation system for pressure reduction and film formation through vacuum rotation |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102580333A true CN102580333A (en) | 2012-07-18 |
| CN102580333B CN102580333B (en) | 2014-04-30 |
Family
ID=46469900
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201210032987.6A Expired - Fee Related CN102580333B (en) | 2012-02-15 | 2012-02-15 | Evaporation system for pressure reduction and film formation through vacuum rotation |
Country Status (2)
| Country | Link |
|---|---|
| CN (1) | CN102580333B (en) |
| WO (1) | WO2013120403A1 (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2013120403A1 (en) * | 2012-02-15 | 2013-08-22 | Fu Lijiang | Vacuum rotation film-forming and depressurizing evaporation system |
| CN104163461A (en) * | 2014-05-05 | 2014-11-26 | 浙江海洋学院 | Novel water treatment purifier |
| CN107285413A (en) * | 2017-08-02 | 2017-10-24 | 六安合益智能家居科技有限公司 | A kind of interim board house sewage-treatment plant |
| CN115888145A (en) * | 2022-12-02 | 2023-04-04 | 台州道致科技股份有限公司 | Control method of isolated electromagnetic induction heating film evaporator |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2553115B (en) | 2016-08-23 | 2021-03-17 | Elmer Edward | Distillation columns |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0275302A (en) * | 1988-09-09 | 1990-03-15 | Hitachi Ltd | Evaporator of rotary blade type |
| CN101239244A (en) * | 2007-02-08 | 2008-08-13 | 中国纺织科学研究院 | Scraper type materiel mixing evaporator |
| CN201676540U (en) * | 2010-02-01 | 2010-12-22 | 张亚宇 | Internal circulation-type scraper film evaporator with hollow spindle |
| CN202105450U (en) * | 2011-05-18 | 2012-01-11 | 华南理工大学 | Scraping plate type microwave vacuum concentration equipment |
| CN202490453U (en) * | 2012-02-15 | 2012-10-17 | 傅利江 | Film-forming and depressurizing evaporation system by vacuum rotation |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE4124337A1 (en) * | 1991-07-23 | 1993-01-28 | Rudolf Pelzer | THICK FILM EVAPORATOR |
| CN2723428Y (en) * | 2004-09-10 | 2005-09-07 | 张培洲 | Large plate type evaporator |
| CN201482226U (en) * | 2009-08-15 | 2010-05-26 | 淄博贝特化工设备有限公司 | Glass lining high-efficiency rotating scraping plate film evaporator |
| CN102580333B (en) * | 2012-02-15 | 2014-04-30 | 傅利江 | Evaporation system for pressure reduction and film formation through vacuum rotation |
-
2012
- 2012-02-15 CN CN201210032987.6A patent/CN102580333B/en not_active Expired - Fee Related
-
2013
- 2013-01-14 WO PCT/CN2013/070405 patent/WO2013120403A1/en active Application Filing
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0275302A (en) * | 1988-09-09 | 1990-03-15 | Hitachi Ltd | Evaporator of rotary blade type |
| CN101239244A (en) * | 2007-02-08 | 2008-08-13 | 中国纺织科学研究院 | Scraper type materiel mixing evaporator |
| CN201676540U (en) * | 2010-02-01 | 2010-12-22 | 张亚宇 | Internal circulation-type scraper film evaporator with hollow spindle |
| CN202105450U (en) * | 2011-05-18 | 2012-01-11 | 华南理工大学 | Scraping plate type microwave vacuum concentration equipment |
| CN202490453U (en) * | 2012-02-15 | 2012-10-17 | 傅利江 | Film-forming and depressurizing evaporation system by vacuum rotation |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2013120403A1 (en) * | 2012-02-15 | 2013-08-22 | Fu Lijiang | Vacuum rotation film-forming and depressurizing evaporation system |
| CN104163461A (en) * | 2014-05-05 | 2014-11-26 | 浙江海洋学院 | Novel water treatment purifier |
| CN107285413A (en) * | 2017-08-02 | 2017-10-24 | 六安合益智能家居科技有限公司 | A kind of interim board house sewage-treatment plant |
| CN115888145A (en) * | 2022-12-02 | 2023-04-04 | 台州道致科技股份有限公司 | Control method of isolated electromagnetic induction heating film evaporator |
| CN115888145B (en) * | 2022-12-02 | 2024-02-20 | 台州道致科技股份有限公司 | Control method of isolated electromagnetic induction heating thin film evaporator |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102580333B (en) | 2014-04-30 |
| WO2013120403A1 (en) | 2013-08-22 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102580333B (en) | Evaporation system for pressure reduction and film formation through vacuum rotation | |
| US20110266132A1 (en) | Air flow-circulation seawater desalination apparatus | |
| CN104495966A (en) | Bubble humidification and heat pump cycle coupled sea water desalination system and process method | |
| CN206463531U (en) | A kind of rose is produced with crystallization enrichment facility | |
| CN105879418A (en) | Horizontal hydraulic shearing thin film spraying MVR evaporating system | |
| CN102765770B (en) | Efficient machine for desalting sea water | |
| CN110072817A (en) | Distilling apparatus with tubular element and its purposes for distilled water | |
| CN106395950A (en) | Sea water desalination method adopting low-temperature multi-effect distillation for producing fresh water through efficient use of heat energy | |
| CN104591327A (en) | Loop heat pipe-type cylindrical solar seawater desalination device | |
| CN202951265U (en) | Efficient evaporating crystallizer | |
| CN102659194B (en) | Distillation-type seawater desalinization device | |
| CN103342397B (en) | Energy-saving low-temperature multi-effect distillation sea water desalination method | |
| CN202490453U (en) | Film-forming and depressurizing evaporation system by vacuum rotation | |
| CN105129890A (en) | Evaporating crystallizer | |
| CN202951276U (en) | Energy-saving crystallizing evaporator | |
| CN108525333A (en) | Liquid vaporising unit and liquid evaporation technique | |
| CN202542898U (en) | Heat pipe type low-temperature multi-effect seawater dilution system | |
| CN104370315A (en) | Novel low-temperature multi-effect seawater desalination evaporator | |
| CN108452542A (en) | Liquid vaporising unit and liquid evaporation technique | |
| CN103241786A (en) | Evaporation system | |
| CN207605382U (en) | A kind of multiple effect counter current vapo(u)rization system | |
| CN202558663U (en) | Distillation type seawater desalting equipment | |
| CN208641777U (en) | Liquid vaporising unit | |
| CN208716883U (en) | A kind of no vapour source room temperature negative pressure sea water distillation plant | |
| CN208193698U (en) | Inward turning heat cycles evaporator and its system for handling brine waste |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140430 Termination date: 20170215 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |