CN204079946U - Combined type solid-state water distilling apparatus - Google Patents

Abstract

The utility model relates to a kind of water distilling apparatus.A kind of combined type solid-state water distilling apparatus, comprise base, be arranged on vaporization wall bucket and the condenser wall bucket of also mutual sheathing on base, be arranged on the pot bucket in vaporization wall bucket and the top cover being arranged on condenser wall bucket top, described base offers leakage fluid dram and steam input aperture, top cover is provided with condensation liquefaction layer, vaporization wall bucket and between condenser wall bucket and base, condenser wall bucket is sealed and matched with being between top cover to mate, vaporization wall bucket and form open top between condenser wall bucket and base, bottom offers the interlayer cavity of tail washings outlet orifice, condenser wall bucket inwall top or top cover inwall are provided with liquid-discharging means of bottle, described condenser wall bucket inwall is provided with multiple tracks annular condensate storage, condensate storage is communicated with conduit respectively, conduit carries out fractionate liquid collection through condenser wall bucket.The application thoroughly can eliminate low alcohol by molecule short-path distillation, avoids the waste of low alcohol, can fully distill.

Description

Combined type solid-state water distilling apparatus

Technical field

The present invention relates to a kind of water distilling apparatus, be specifically related to a kind of combined type solid-state water distilling apparatus being applied to solid state class unstrained spirits material.

Background technology

In the brewing process of wine, distillation is one important operation, solid-state wine unstrained spirits by fermentation needs to be separated from fragrant unstrained spirits by alcohol through distillation, but traditional white liquor distilling is because the structure of distillation plant " rice steamer " also exists many weak points, thus cause the object that cannot reach thoroughly distillation in still-process.

Its shortcoming existed of traditional distillation plant is: 1, rice steamer distillation cannot realize thoroughly distillating of fragrance matter, and the wine unstrained spirits fragrance matter shown as through distillation retains too much, even still fragrance is pure for the vinasse abandoned distilled.

2, the distillation of rice steamer equipment cannot by the wine of different boiling and lipid material taxonomic revision out, what cause that white wine can be rough except foreshot, wine tail and wine body comes respectively, the composition that in wine body, some is harmful to HUMAN HEALTH cannot be removed, as: cause dry mouth and tougue, dizzy uncomfortable and some trace ingredientss etc. can paid no attention to human tissue cell after the farm chemical ingredients existed in liquor-making raw material, people drink.

3, the single layer structure of rice steamer equipment, rice steamer outer wall is exposed in physical environment completely, and area of dissipation is excessive, and the distance between wine steam to condenser is excessive, thus forces vapor pressure to fall raising, causes highly energy-consuming.

4, rice steamer equipment contacts with physical environment due to outer wall, causing rice steamer inwall wine steam to meet condensation ties dirty along inwall, and the hot steam of meeting bottom is again up, again and again, low alcohol is caused to draw tail long, Zeng Gai is triangular structure, and rice steamer cover outer wall is same and physical environment temperature difference is comparatively large, causes along inwall dirty, owing to generally having water seal between rice steamer pot and rice steamer lid, now, wine flows in the water of water seal, is the faulty stroke in calligraphy or painting of solid state distillation rice steamer.

5, the vapor temperature of current rice steamer equipment is generally about 100 DEG C, be applicable to alcoholic ingredient volume distillation temperature, but the prior meaning of white liquor distilling is Titian, the boiling point of some important lipid materials is all more than 100 °, therefore be difficult to extract, and for traditional rice steamer, even if pass into the Extracting temperature of lipid material, the seal approach of existing rice steamer and structure design still can not realize.Wherein water seal and silicone rubber seal all can not work under hot conditions again.

6, the distillation of scope far from solid spirit of solid state class distillation is belonged to, as the extraction of plant spices, the extraction of some composition of farm crop, the extraction of Chinese herbal medicine effective ingredients, also has the extraction of natural pigments, some tea perfume, the fragrance of a flower, spearmint oil, lavandula angustifolias etc. all need effective control of different distillation temperatures and condensing temperature, and traditional rice steamer cannot realize regulating and temperature control from subzero tens degree of temperature to a few Baidu above freezing.

Summary of the invention

The object of the invention is for above-mentioned Problems existing and deficiency, a kind of lipid material that can effectively extract in wine unstrained spirits is provided, thoroughly can distills the effective constituent of unstrained spirits material and independent separated and collected, and separation can be carried out to oxious component to discharge, the distillation of other solid state class can also be applicable to, by molecule short-path distillation technology and the combined type solid-state water distilling apparatus time heating up in a steamer distillation technique and combine.

For achieving the above object, the technical scheme taked is:

A kind of combined type solid-state water distilling apparatus, comprise base, be arranged on vaporization wall bucket and the condenser wall bucket of also mutual sheathing on base, be arranged on the pot bucket in vaporization wall bucket and the top cover being arranged on condenser wall bucket top, described base offers leakage fluid dram and steam input aperture, top cover is provided with condensation liquefaction layer, vaporization wall bucket and between condenser wall bucket and base, condenser wall bucket is sealed and matched with being between top cover to mate, vaporization wall bucket and form open top between condenser wall bucket and base, bottom offers the interlayer cavity of tail washings outlet orifice, condenser wall bucket inwall top or top cover inwall are provided with liquid-discharging means of bottle, liquid is guided into vaporization wall bucket outside wall surface by liquid-discharging means of bottle, described condenser wall bucket inwall is provided with multiple tracks annular condensate storage, condensate storage is communicated with conduit respectively, conduit carries out fractionate liquid collection through condenser wall bucket.

Described top cover offers steam to return and heat up in a steamer hole, steam returns and heats up in a steamer hole and return distillate conduit by steam and be communicated with Pistonless compressor, the outlet side of Pistonless compressor is communicated with in the distillation cavity of pot bottom of the barrel, return on distillate conduit at the described coconnected steam in Pistonless compressor outlet side and be provided with T-valve, the 3rd end of described T-valve is communicated with high-temperature vapour producer.

Described liquid-discharging means of bottle is the annular diversion trench being arranged on condenser wall bucket inwall top or top cover inner wall lower, and the outer of annular diversion trench is near vaporization wall bucket outer wall and leave gap.

The bottom of described annular diversion trench offers liquid and returns and heat up in a steamer hole, liquid returns and heats up in a steamer hole and return distillate conduit by liquid and be communicated with liquid-storing box, liquid returns on distillate conduit and is provided with control valve, liquid-storing box is also communicated with volume pump, the water side of volume pump is connected with T-valve, the other two ends of this T-valve are connected to backflow transport pipe and molecule short-path distillation transport pipe, described backflow transport pipe is communicated with the liquid distributor be arranged in pot bottom of the barrel distillation cavity, described molecule short-path distillation transport pipe passes and is communicated with and is arranged on the shower nozzle of condenser wall bucket top towards vaporization wall bucket outside wall surface, between liquid distributor and the steam input aperture of bottom, be provided with structured filling material layer, described shower nozzle is uniformly distributed along condenser wall bucket surrounding, described liquid distributor helically plate-like, uniformly on liquid distributor offers liquid distributing hole.

Described molecule short-path distillation transport pipe is also provided with T-valve, 3rd end bypass line of described T-valve is provided with a pillar fractionator, described pillar fractionator comprises vaporization wall bucket, be set in the two condenser wall buckets in outside in vaporization wall bucket, and be arranged on the base plate of bottom, two condenser wall buckets are all arranged on multiple tracks annular condensate storage, described condensate storage is communicated with conduit, described base plate offers leakage fluid dram, described bypass line end is the annular thrust-augmenting nozzle offering a series of hole, annular thrust-augmenting nozzle is arranged on vaporization wall bucket top.

The refrigerant of described condensation liquefaction layer for passing in the liquefaction cavity that is arranged on liquefaction housing outside top cover, liquefaction housing and top cover and formed and the cavity that liquefies; Or described liquidized layer is the refrigerant that passes in the refrigerant storage tanks of the baffle plate composition be arranged on top cover and refrigerant storage tanks; Or described condensation liquefaction layer is the top cover be made up of stainless steel corrugated-type board, and passes into refrigerant in the passage of this stainless steel corrugated-type board.

Described vaporization wall bucket comprises housing and is arranged at least one the heating agent unit on inner walls face, each heating agent unit can control separately the temperature of this annular vaporization shell area, and described heating agent unit comprises the heating agent pipeline be arranged on this inner walls face, heating agent unit area and the heating agent passing into heating agent pipeline.

Described condenser wall bucket comprise with hollow cavity condensation housing and be arranged on refrigerant unit in hollow cavity, described refrigerant unit is the refrigerant directly passed in hollow cavity; Or described refrigerant unit is be arranged in the refrigerant pipe in condensation housing, passes into refrigerant in described refrigerant pipe.

Described vaporization wall bucket and condenser wall bucket are in barrel-shaped stainless steel corrugated-type board, the stainless steel corrugated-type board of described vaporization wall bucket comprises at least one heating agent unit, multiple tracks stainless steel corrugated-type board passage in described single heating agent unit is connected, and the stainless steel corrugated-type board passage of each different heating agent unit is separate; Passage in the stainless steel corrugated-type board of described condenser wall bucket for being connected in series or being connected in parallel, and has passed into refrigerant in its passage.

The top of described pot bucket is provided with outwardly outer, pot bucket is being vaporized on wall bucket by outer hanging, on the outer of pot bucket and the bottom of pot bucket is equipped with hanger, the clamping of pot bucket inside bottom is provided with the hollow structure taper unstrained spirits material preventing material from killing and loosens bucket, and described top cover is provided with thermometer.

Adopt technique scheme, acquired beneficial effect is:

1. the application adopts molecule short-path distillation technical functionality, two formula of heating up in a steamer is distilled and can all be distillated by the wine in solid wine unstrained spirits in the short period of time, not a large amount of low tail wine of traditional liquor distillation generation, the application adopts Conventional espresso and molecule short-path distillation to combine, in whole distillation process process, all the time high-quality high wine can be produced, the very large adjustment that the ratio of high wine and low alcohol is obtained, there is too much low tail wine in the phase after distillation to avoid traditional distil process, causes great waste;

3. two formula white liquor distilling rice steamer that heats up in a steamer have employed liquor condensation and returns and heat up in a steamer operation or/and steam returns heat up in a steamer operation, by the wine after distillation is returned steaming again, alcohol dissolubility fat in wine unstrained spirits more can be dissolved in wine and take out of, add the fragrance of white wine, mouthfeel, comparatively traditional liquor better quality, two formula white liquor distilling that heats up in a steamer adopts molecule short-path distillation method, material in wine can be separated step by step, material harmful in white wine can be removed from wine by this separation means, the headache caused after drinking can be avoided, dry, and the fluidizer contained in wine and farm chemical ingredients, make the health care wine that white wine becomes real,

4. two formula white liquor distilling rice steamer that heats up in a steamer is by the improvement of structure and design, from wine steam to being cooled to liquid collecting, 3mm is reduced to from original wine steam stroke 300cm, the distance of this process shortens greatly, reduce Pressure Drop, further increase and steam wine efficiency, simultaneously, traditional distillation is needed to carry out pouring yellow water, dehydration, increase rice husk as auxiliary material, alleviated the humidity of wine unstrained spirits by profit grain, and the application is distilled by liquid molecule short distance, break original vapor liquid equilibrium, not by the impact of wine unstrained spirits humidity, more wine can be extracted, improve quality and the number of degrees of wine;

5. the application can also be applied to the industries such as fiber-like resource, spices, as the sufficient wheat-straw, lignosulfite etc. of originating, fiber in these raw materials distills in existing column plate type distilling machinery, easily result in blockage, the problem of difficult treatment, and the problem that effectively can make up tower distillation inconvenience process fibre-bearing fermented liq many especially of the application and Conventional espresso rice steamer cannot realize a difficult problem for rectifying;

6. due to after traditional white liquor distilling, need to open pot cover and carry out steaming grain several tens minutes again, its a large amount of steaming grain steam cannot well be utilized, the application returns distillate conduit by steam and is connected in other retort and distills, substantially increase the utilization ratio of the energy, after steaming grain, steaming grain is also needed to dispel the heat, then again ferment, tradition carries out spreading heat radiation out, the application extracts freezing air by steam compressed pump from the steam input aperture base and carries out radiating and cooling, substantially increases working efficiency, reduces artificial labor force;

7. the application adopts food grade stainless steel corrugated-type board to carry out making condenser wall bucket and vaporization wall bucket, its heat transport element stainless steel corrugated-type board, it possesses multiple vaporization zone, multiple heating agent, regional carries out separately molecule short-path distillation temperature and controls, effectively can extract various required material, hierarchical, high-quality distillation object can be reached.

Accompanying drawing explanation

Fig. 1 is the structural representation of combined type solid-state water distilling apparatus of the present invention.

Fig. 2 is one of structure for amplifying schematic diagram of Fig. 1 centre circle A.

Fig. 3 is the structure for amplifying schematic diagram two of Fig. 1 centre circle A.

Fig. 4 is the structural representation of liquid distributor.

Fig. 5 is the structural representation of stainless steel corrugated-type board.

Fig. 6 be in Fig. 5 A-A to structural representation.

Fig. 7 be in Fig. 5 B-B to structural representation.

Fig. 8 is the heating agent modular construction schematic diagram of vaporization wall bucket.

Fig. 9 is the structural representation of pillar fractionator.

Sequence number in figure: 1 is base, 2 is vaporization wall bucket, 3 is condenser wall bucket, 4 is pot bucket, 5 is top cover, 6 is leakage fluid dram, 7 is steam input aperture, 8 is tail washings outlet orifice, 9 is interlayer cavity, 10 is annular diversion trench, 11 is condensate storage, 12 is conduit, 13 heat up in a steamer hole for steam returns, 14 return distillate conduit for steam, 15 is Pistonless compressor, 16 is T-valve, 17 return distillate conduit for liquid, 18 is liquid-storing box, 19 is volume pump, 20 is control valve, 21 is liquid distributor, 22 is structured filling material layer, 23 is heating agent pipeline, 24 is refrigerant pipe, 25 is outer, 26 to loosen bucket for unstrained spirits material, 27 is hanger, 28 is baffle plate, 29 is stainless steel corrugated-type board, 30 is heating agent unit, 31 is stainless steel corrugated-type board passage, 32 is shower nozzle, 33 molecule short-path distillation transport pipes, 34 is backflow transport pipe, 35 is bypass line, 36 is pillar fractionator, 37 is base plate, 38 is annular thrust-augmenting nozzle, 39 is high-temperature vapour producer, 40 is thermometer.

Embodiment

Below in conjunction with accompanying drawing, the specific embodiment of the present invention is elaborated.

Embodiment one: see Fig. 1, Fig. 2, Fig. 4, a kind of combined type solid-state water distilling apparatus, comprise base 1, be arranged on vaporization wall bucket 2 and the condenser wall bucket 3 of also mutual sheathing on base 1, be arranged on the pot bucket 4 in vaporization wall bucket 2 and the top cover 5 being arranged on condenser wall bucket 3 top, described base 1 offers leakage fluid dram 6 and vapor inlet port 7, condensation liquefaction layer is provided with outside top cover 5, vaporization wall bucket 2 and between condenser wall bucket 3 and base 1, be to mate between condenser wall bucket 3 with top cover 5 and be sealed and matched, vaporization wall bucket 2 and form open top between condenser wall bucket 3 and base 1, bottom offers the interlayer cavity 9 of tail washings outlet orifice 8, condenser wall bucket 3 inwall top is provided with liquid-discharging means of bottle, liquid is guided into vaporization wall bucket outside wall surface by liquid-discharging means of bottle, described liquid-discharging means of bottle is the annular diversion trench 10 being arranged on condenser wall cylinder 3 inwall top, the outer of annular diversion trench 10 is near vaporization wall bucket outer wall and leave gap, liquid is guided into vaporization wall bucket 2 outside wall surface by annular diversion trench 10, described condenser wall bucket 3 inwall is provided with multiple tracks annular condensate storage 11, condensate storage 11 is communicated with conduit 12 respectively, conduit 12 carries out fractionate liquid collection through condenser wall bucket 3.

The principle of work of the present embodiment is: contained by wine unstrained spirits in pot bucket, pass into high-temperature vapour by steam input aperture to distill, white wine steam rises, the condensation liquefaction layer that top cover is arranged is used for the white wine steam cooling that the distillation of wine unstrained spirits produces to liquefy, and flow to interlayer cavity along cover wall, liquid is guided first to flow to vaporization wall bucket by annular diversion trench, by the heating agent passed in vaporization wall bucket, form high-temperature evaporation hot wall, carry out molecule short-path distillation, the molecule overflowed of now vaporization wall bucket wall being vaporized directly flies on condenser wall bucket wall, and liquefaction is collected, it does not get back to the possibility on vaporization wall bucket wall, belong to irreversible still-process, by being successively set on the separation of the side stream of the condensate storage on condenser wall bucket wall, the wine of high density, high-quality can be isolated, avoid the appearance of a large amount of low tail wine, break traditional vapor liquid equilibrium, greatly can improve yield and the extracting rate of the fat in fermented wine unstrained spirits simultaneously.

Embodiment two: see Fig. 1, Fig. 3, Fig. 4, the structure of the present embodiment is substantially identical with embodiment one, and something in common no longer repeats, and its difference is: described annular diversion trench 10 is arranged on top cover inner wall lower.

Embodiment three: see Fig. 1-Fig. 4, the structure of the present embodiment is substantially identical with embodiment one, something in common no longer repeats, its difference is: described top cover 5 offers steam and return and heat up in a steamer hole 13, steam returns and heats up in a steamer hole 13 and return distillate conduit 14 by steam and be communicated with Pistonless compressor 15, the outlet side of Pistonless compressor 15 is returned distillate conduit 13 by steam and is communicated with in the retort cavity of pot bottom of the barrel, steam returns on distillate conduit 13 and is also communicated with high-temperature vapour producer by T-valve, can superheated vapo(u)r be passed into, lipid material is extracted.

In still-process, fat in fermented wine unstrained spirits is difficult to directly to be dissolved in the water vapour passed into, and the extracting rate of the fat in fermented wine unstrained spirits will be caused so very low, cause the waste of a large amount of fat, therefore, returned by interpolation steam and heat up in a steamer operation, the phase before it is distilled, in the condensation liquefaction layer of top cover, do not pass into refrigerant, namely directly steam liquefaction is not carried out, but advanced steam returns and heats up in a steamer, make alcohol dissolubility liposoluble in fermented wine unstrained spirits in wine steam, thus substantially increase the quality of wine.

Embodiment four: see Fig. 1-Fig. 3, the structure of the present embodiment is substantially identical with embodiment one or two or three, something in common no longer repeats, its difference is: the bottom of described annular diversion trench 10 offers liquid and returns and heat up in a steamer hole, liquid returns and heats up in a steamer hole and return distillate conduit 17 by liquid and be communicated with liquid-storing box 18, liquid returns on distillate conduit 17 and is provided with control valve 20, liquid-storing box 18 is also communicated with volume pump 19, the water side of volume pump 19 is connected with T-valve 16, the other two ends of this T-valve 16 are connected to backflow transport pipe 34 and molecule short-path distillation transport pipe 33, described backflow transport pipe 34 is communicated with the liquid distributor 21 being arranged on and distilling bottom pot bucket 4 in cavity, described molecule short-path distillation transport pipe 33 passes and is communicated with and is arranged on the shower nozzle 32 of condenser wall bucket 3 top towards vaporization wall bucket 2 outside wall surface, between liquid distributor 21 and the steam input aperture 7 of bottom, be provided with structured filling material layer 22, described shower nozzle 32 is uniformly distributed along condenser wall bucket 3 surrounding, described liquid distributor 21 helically plate-like, uniformly on liquid distributor 21 offers liquid distributing hole.

In still-process, fat in fermented wine unstrained spirits is difficult to directly to be dissolved in the water vapour passed into, the extracting rate of the fat in fermented wine unstrained spirits will be caused so very low, cause the waste of a large amount of fat, in addition cannot well utilize for the low alcohol produced in traditional still-process, cause waste, the application is returned by increase liquid and heats up in a steamer operation, low alcohol can be re-used, by low alcohol being sprayed into again in retort cavity, the structured packing of low alcohol and steam is carried out by structured filling material layer, ethanol in low alcohol is gasified, carry out distilling the extraction carrying out fat, and the water in low alcohol is discharged from leakage fluid dram downwards, simultaneously at the distillation initial stage, also can return as the steam in embodiment three and heat up in a steamer operation, be reentered the extraction carrying out fat in retort by the wine dissolved distillate.

Simultaneously for the wine liquid liquefied from top cover, because whole solid state distillation device is steady not, there will be the situation that liquid is amesiality in annular diversion trench, therefore, after liquid is drawn, re-start sprinkler, greatly can not only improve the efficiency of molecule short-path distillation, more evenly can improve the quality of molecule short-path distillation simultaneously.

Embodiment five: see Fig. 1-Fig. 4, the structure of the present embodiment is substantially identical with embodiment one, something in common no longer repeats, and its difference is: the refrigerant of described condensation liquefaction layer for passing in the liquefaction cavity that is arranged on liquefaction housing outside top cover, liquefaction housing and top cover and formed and the cavity that liquefies; Or described liquidized layer is be arranged on the refrigerant passed in refrigerant storage tanks and refrigerant storage tanks that baffle plate 28 on top cover 4 forms; Or described condensation liquefaction layer is the top cover be made up of stainless steel corrugated-type board, and passes into refrigerant in the passage of this stainless steel corrugated-type board.

Embodiment six: see Fig. 1-Fig. 4, the structure of the present embodiment is substantially identical with embodiment one, something in common no longer repeats, its difference is: on the outer 25 of described pot the bucket 4 and bottom of pot bucket 4 is equipped with hanger 27, facilitate lifting and the handling of pot bucket, directly can hang the hanger 27 bottom pot bucket 4 when unloading simultaneously, directly unload, the clamping of pot bucket 4 inside bottom is provided with the hollow structure taper unstrained spirits material preventing material from killing to loosen bucket 26, described top cover 5 is provided with thermometer 40, to be loosened by unstrained spirits material the design of bucket, effectively can solve and kill phenomenon in mechanical charging process, cause airproof problem.

Embodiment seven: see Fig. 1-Fig. 4, Fig. 9, the structure of the present embodiment is substantially identical with embodiment four, something in common no longer repeats, its difference is: described molecule short-path distillation transport pipe 33 is also provided with T-valve 16, 3rd end bypass line 35 of described T-valve 16 is provided with a pillar fractionator 36, described pillar fractionator comprises vaporization wall bucket 2, be set in the two condenser wall buckets 3 in outside in vaporization wall bucket 2, and be arranged on the base plate 37 of bottom, two condenser wall buckets 3 are all arranged on multiple tracks annular condensate storage 11, described condensate storage 11 is communicated with conduit 12, described base plate 37 offers leakage fluid dram 6, described bypass line 35 end is the annular thrust-augmenting nozzle 38 offering a series of hole, annular thrust-augmenting nozzle 38 is arranged on vaporization wall bucket 2 top, by the wine steam of condensation being introduced the pillar fractionator 36 of sectionalization, the Extraction and separation of the wine of refinement more can be carried out, to carry out the further segmentation of all kinds of material.

Embodiment eight: see Fig. 1-Fig. 4, the structure of the present embodiment is substantially identical with embodiment three, something in common no longer repeats, its difference is: the steam of described Pistonless compressor 15 outlet side returns the T-valve 16 on distillate conduit 14, it can carry out steam and return and heat up in a steamer operation, in addition, Conventional espresso rice steamer is after distillation completes, also to take off lid and steam grain several tens minutes, its a large amount of high temperature steams grain steam directly discharged to air, cause the waste of the energy, high-temperature gas directly can be introduced in other retort by T-valve and distill by the application, greatly can not only reduce the waste of the energy, also can improve the extracting rate of fat simultaneously, improve the quality of wine.

Simultaneously need to spread heat radiation out after steaming grain, and the application directly sucks freezing air by steam compressed pump and directly dispels the heat, and decreases labour intensity, also convenient filler operation of again fermenting, greatly reduces the labour intensity of workman, improve working efficiency.

Embodiment nine: see Fig. 1-Fig. 4, the structure of the present embodiment is substantially identical with embodiment one, something in common no longer repeats, its difference is: described vaporization wall bucket 2 comprises housing and is arranged at least one the heating agent unit on inner walls face, each heating agent unit can control separately the temperature of this annular vaporization shell area, and described heating agent unit comprises the heating agent pipeline 23 be arranged on this inner walls face, heating agent unit area and the heating agent passing into heating agent pipeline 23.Described condenser wall bucket 3 comprise with hollow cavity condensation housing and be arranged on refrigerant unit in hollow cavity, described refrigerant unit is the refrigerant directly passed in hollow cavity, or described refrigerant unit is the refrigerant pipe 24 be arranged in condensation housing, passes into refrigerant in described refrigerant pipe 24.

Embodiment ten: see Fig. 1-Fig. 8, the structure of the present embodiment is substantially identical with embodiment one, something in common no longer repeats, its difference is: described vaporization wall bucket 2 and condenser wall bucket 3 are the stainless steel corrugated-type board 29 in tubular, the stainless steel corrugated-type board of described vaporization wall bucket 2 comprises at least one heating agent unit 30, multiple tracks stainless steel corrugated-type board passage 31 in described single heating agent unit 30 is connected, and the stainless steel corrugated-type board passage 31 of each different heating agent unit 30 is separate; Passage in the stainless steel corrugated-type board 29 of described condenser wall bucket 3 for being connected in series or being connected in parallel, and has passed into refrigerant in its passage.

The application adopts stainless steel corrugated-type board can carry out hyperchannel, multi-fluid to carry out heat exchange molecule short-path distillation simultaneously, adopt the heating agent of multiple differing temps, thus reach the object be separated one by one according to different materials.

Claims (10)

1. a combined type solid-state water distilling apparatus, it is characterized in that, comprise base, be arranged on vaporization wall bucket and the condenser wall bucket of also mutual sheathing on base, be arranged on the pot bucket in vaporization wall bucket and the top cover being arranged on condenser wall bucket top, described base offers leakage fluid dram and steam input aperture, top cover is provided with condensation liquefaction layer, vaporization wall bucket and between condenser wall bucket and base, condenser wall bucket is sealed and matched with being between top cover to mate, vaporization wall bucket and form open top between condenser wall bucket and base, bottom offers the interlayer cavity of tail washings outlet orifice, condenser wall bucket inwall top or top cover inwall are provided with liquid-discharging means of bottle, liquid is guided into vaporization wall bucket outside wall surface by liquid-discharging means of bottle, described condenser wall bucket inwall is provided with multiple tracks annular condensate storage, condensate storage is communicated with conduit respectively, conduit carries out fractionate liquid collection through condenser wall bucket.

2. combined type solid-state water distilling apparatus according to claim 1, it is characterized in that, described top cover offers steam to return and heat up in a steamer hole, steam returns and heats up in a steamer hole and return distillate conduit by steam and be communicated with Pistonless compressor, the outlet side of Pistonless compressor is communicated with in the distillation cavity of pot bottom of the barrel, return on distillate conduit at the described coconnected steam in Pistonless compressor outlet side and be provided with T-valve, the 3rd end of described T-valve is communicated with high-temperature vapour producer.

3. combined type solid-state water distilling apparatus according to claim 1, it is characterized in that, described liquid-discharging means of bottle is the annular diversion trench being arranged on condenser wall bucket inwall top or top cover inner wall lower, and the outer of annular diversion trench is near vaporization wall bucket outer wall and leave gap.

4. combined type solid-state water distilling apparatus according to claim 3, it is characterized in that, the bottom of described annular diversion trench offers liquid and returns and heat up in a steamer hole, liquid returns and heats up in a steamer hole and return distillate conduit by liquid and be communicated with liquid-storing box, liquid returns on distillate conduit and is provided with control valve, liquid-storing box is also communicated with volume pump, the water side of volume pump is connected with T-valve, the other two ends of this T-valve are connected to backflow transport pipe and molecule short-path distillation transport pipe, described backflow transport pipe is communicated with the liquid distributor be arranged in pot bottom of the barrel distillation cavity, described molecule short-path distillation transport pipe passes and is communicated with and is arranged on the shower nozzle of condenser wall bucket top towards vaporization wall bucket outside wall surface, between liquid distributor and the steam input aperture of bottom, be provided with structured filling material layer, described shower nozzle is uniformly distributed along condenser wall bucket surrounding, described liquid distributor helically plate-like, uniformly on liquid distributor offers liquid distributing hole.

5. combined type solid-state water distilling apparatus according to claim 4, it is characterized in that, described molecule short-path distillation transport pipe is also provided with T-valve, 3rd end bypass line of described T-valve is provided with a pillar fractionator, described pillar fractionator comprises vaporization wall bucket, be set in the two condenser wall buckets in outside in vaporization wall bucket, and be arranged on the base plate of bottom, two condenser wall buckets are all arranged on multiple tracks annular condensate storage, described condensate storage is communicated with conduit, described base plate offers leakage fluid dram, described bypass line end is the annular thrust-augmenting nozzle offering a series of hole, annular thrust-augmenting nozzle is arranged on vaporization wall bucket top.

6. combined type solid-state water distilling apparatus according to claim 1, is characterized in that, the refrigerant of described condensation liquefaction layer for passing in the liquefaction cavity that is arranged on liquefaction housing outside top cover, liquefaction housing and top cover and formed and the cavity that liquefies; Or described liquidized layer is the refrigerant that passes in the refrigerant storage tanks of the baffle plate composition be arranged on top cover and refrigerant storage tanks; Or described condensation liquefaction layer is the top cover be made up of stainless steel corrugated-type board, and passes into refrigerant in the passage of this stainless steel corrugated-type board.

7. combined type solid-state water distilling apparatus according to claim 1 or 5, it is characterized in that, described vaporization wall bucket comprises housing and is arranged at least one the heating agent unit on inner walls face, each heating agent unit can control separately the temperature of this annular vaporization shell area, and described heating agent unit comprises the heating agent pipeline be arranged on this inner walls face, heating agent unit area and the heating agent passing into heating agent pipeline.

8. combined type solid-state water distilling apparatus according to claim 1 or 5, it is characterized in that, described condenser wall bucket comprise with hollow cavity condensation housing and be arranged on refrigerant unit in hollow cavity, described refrigerant unit is the refrigerant directly passed in hollow cavity; Or described refrigerant unit is be arranged in the refrigerant pipe in condensation housing, passes into refrigerant in described refrigerant pipe.

9. combined type solid-state water distilling apparatus according to claim 1 or 5, it is characterized in that, described vaporization wall bucket and condenser wall bucket are in barrel-shaped stainless steel corrugated-type board, the stainless steel corrugated-type board of described vaporization wall bucket comprises at least one heating agent unit, multiple tracks stainless steel corrugated-type board passage in described single heating agent unit is connected, and the stainless steel corrugated-type board passage of each different heating agent unit is separate; Passage in the stainless steel corrugated-type board of described condenser wall bucket for being connected in series or being connected in parallel, and has passed into refrigerant in its passage.

10. combined type solid-state water distilling apparatus according to claim 1, it is characterized in that, the top of described pot bucket is provided with outwardly outer, pot bucket is being vaporized on wall bucket by outer hanging, on the outer of pot bucket and the bottom of pot bucket is equipped with hanger, the clamping of pot bucket inside bottom is provided with the hollow structure taper unstrained spirits material preventing material from killing and loosens bucket, and described top cover is provided with thermometer.