CN206666493U - Separated device and apply its white wine impurity removing equipment - Google Patents
Separated device and apply its white wine impurity removing equipment Download PDFInfo
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- CN206666493U CN206666493U CN201720401841.2U CN201720401841U CN206666493U CN 206666493 U CN206666493 U CN 206666493U CN 201720401841 U CN201720401841 U CN 201720401841U CN 206666493 U CN206666493 U CN 206666493U
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Abstract
The utility model provides a kind of separated device and applies its white wine impurity removing equipment, is related to the technical field of material separation.Separated device provided by the utility model includes boiler and condenser, and the bottom of condenser is provided with intercepter plate, the side wall of intercepter plate and condenser forms a reservoir, in addition the also external collector of reservoir；Liquid in boiler is risen in condenser in vapour form, after being contacted with condenser side wall, can be condensed into liquid along condenser side wall, liquid flows down along side wall and is trapped plate and intercepts, collect in reservoir, and then enter separate substance collector, it is achieved thereby that the process of separated.The structure design that the utility model passes through uniqueness, there is provided a kind of new separated device, alleviate the problem of distiller condenser structure is single in the prior art.
Description
Technical field
Material separation technology field is the utility model is related to, more particularly, to a kind of separated device and using the white of its
Wine impurity removing equipment.
Background technology
Distillation, refer to using volatile difference between each component in liquid mixture, and the process that component is separated.Steam
For cut from addition to applied to scientific research, the life with people is also closely bound up, is widely used in food, medicine processing,
Especially during drink processing.By taking liquor production as an example, in the production fermentation process of white wine, distillation serves heavy to closing
The effect wanted.It is that steam caused by liquid boiling is imported into condensing unit, and be allowed to cold the step of most critical in separated
But liquid is condensed into.
In the prior art, condensing unit typically uses condenser pipe, and condenser pipe is generally made up of thinner tubule, outside tubule
Portion is also typically provided with thicker sleeve pipe, and cooling material is filled between tubule and sleeve pipe, is turned into causing the steam in tubule to condense
Liquid.In addition, there is some improvement carried out to condenser pipe, such as helical form or " S " shape are formed it into, to increase limited sky
Between interior condenser tube length, so as to improve the efficiency of condensation.
But howsoever improve, design of the people to condensing unit can not break through the barrier of condenser pipe all the time；Except this it
Outside, condenser pipe in use, be there are problems that all the time, for example, due to condenser pipe be typically designed to helical form or
" S " shape, cause its extremely difficult cleaning, especially when using condenser pipe during food processing, be even more difficult to monitor condenser pipe
Interior quality security problem.It is therefore desirable to break through the barrier of condenser pipe, a kind of new separated device is designed.
In view of this, it is special to propose the utility model.
Utility model content
First purpose of the present utility model is to provide a kind of separated device, to alleviate distillation point in the prior art
The technical problem single from apparatus structure；Second purpose of the present utility model is to provide a kind of white wine impurity removing equipment.
The utility model provides a kind of separated device, and the separated device includes：
Boiler, and condenser of the through connection above the boiler；
The condenser has the shape that middle part is expanded；
The condenser bottom sets the oriented inclined intercepter plate of condenser side, the side wall of the condenser and institute
State intercepter plate and form reservoir, the reservoir can be stored along the dirty liquid of side wall condensation；
The reservoir is circumscribed with separate substance collector.
Further, the top of the condenser is provided with open top, and the open-topped diameter is less than the condensation
The diameter for the connecting portion that device is connected with the boiler.
Further, the diameter proportion of the open-topped diameter and the connecting portion is 1：2-4.
Further, the side wall include into curvilinear plane upper portion side wall, the lower sides in the face that is in line, and it is described on
Portion's side wall and the pars intermedia side wall of the lower sides junction；The pars intermedia side wall is the maximum gauge of the condenser
Place.
Further, the diameter proportion of the diameter of the pars intermedia side wall and the connecting portion is 1.5-3：1.
Further, the diameter proportion of the diameter of the pars intermedia side wall and the connecting portion is 2：1.
Further, the condenser external is provided with water circle device.
Further, it is provided with water circle device outside the boiler.
In addition, the utility model additionally provides a kind of white wine impurity removing equipment, the white wine impurity removing equipment includes：The distillation
Separator, the clarifier being connected with the open top, and the condensing collector being connected with the clarifier.
Further, it is provided with acticarbon in the clarifier.
Separated device provided by the utility model includes boiler and condenser, and the bottom of condenser, which is provided with, dams
The side wall of plate, intercepter plate and condenser forms a reservoir, in addition the also external collector of reservoir；Liquid in boiler
Body is risen in condenser in vapour form, after being contacted with condenser side wall, can be condensed into liquid, liquid edge along condenser side wall
Side wall flows down and is trapped plate interception, collects in reservoir, and then enters separate substance collector, it is achieved thereby that distillation point
From process.The structure design that the utility model passes through uniqueness, there is provided a kind of new separated device, alleviate existing
The problem of distiller condenser structure is single in technology.
Brief description of the drawings
, below will be right in order to illustrate more clearly of the utility model embodiment or technical scheme of the prior art
The required accompanying drawing used is briefly described in embodiment or description of the prior art, it should be apparent that, describe below
In accompanying drawing be some embodiments of the present utility model, for those of ordinary skill in the art, do not paying creativeness
On the premise of work, other accompanying drawings can also be obtained according to these accompanying drawings.
Fig. 1 is the overall structure diagram of the separated device of the utility model the first embodiment offer；
Fig. 2 is the sectional view of condenser in the condensing unit that the utility model the first embodiment provides；
Fig. 3 is the schematic diagram of boiler in the condensing unit that the utility model the first embodiment provides；
Fig. 4 is the structural representation for the white wine knot screen that second of embodiment of the utility model provides；
Fig. 5 is the structural representation for the clarifier that second of embodiment of the utility model provides.
Icon：1- boilers；11- boiler charging apertures；2- condensers；21- intercepter plates；22- side walls；On 221-
Portion's side wall；222- lower sides；223- pars intermedia side walls；23- reservoirs；24- open tops；25- liquid storage channel openings；
3- connecting portions；4- separate substance collectors；5- clarifiers；51- clarifier imports；52- clarifiers export；53- gaseous states
It is separated by filtration tower；The condensers of 54- first；The condensers of 55- second；56- harmful substance condenser pipes；6- condensing collectors.
Embodiment
The technical solution of the utility model is clearly and completely described below in conjunction with embodiment, it is clear that described
Embodiment be a part of embodiment of the utility model, rather than whole embodiment.Based in the utility model
Embodiment, the every other embodiment party that those of ordinary skill in the art are obtained under the premise of creative work is not made
Formula, belong to the scope of the utility model protection.
, it is necessary to explanation in description of the present utility model, such as occur term " on ", " under ", " vertical ", " interior ",
The orientation or position relationship of instructions such as " outer " are based on orientation shown in the drawings or position relationship, are for only for ease of and describe this reality
With new and simplify description, rather than instruction or imply that signified device or element there must be specific orientation, with specific
Azimuth configuration and operation, therefore it is not intended that to limitation of the present utility model.In addition, term " first ", " second " are only used for
Purpose is described, and it is not intended that instruction or hint relative importance.
, it is necessary to which explanation, unless otherwise clearly defined and limited, term such as occurs in description of the present utility model
" installation ", " connected ", " connection " should be interpreted broadly, for example, it may be fixedly connected or be detachably connected, or one
Connect body；Can be mechanical connection or electrical connection；Can be joined directly together, can also be indirect by intermediary
It is connected, can is the connection of two element internals.For the ordinary skill in the art, on being understood with concrete condition
State concrete meaning of the term in the utility model.
Distilling apparatus of the prior art, generally use condenser pipe condense to the gas of evaporation, and structure is very single,
The improvement carried out to it is also to improve the effect of condensation by changing the length in the confined space of condenser pipe mostly；And
Condenser pipe has the characteristics of easily blocking, hardly possible cleaning, is particularly applied in food processing process, and condenser pipe is even more easily to grow carefully
Bacterium, it is not easy to carry out quality and safety control to the overall process of food processing.Two kinds of embodiments provided by the utility model are exactly pair
The problem of distilling apparatus structure is single in the prior art and the improvement proposed, both embodiments will be carried out below detailed
Thin explanation.
Fig. 1 is the overall structure diagram for the separated device that the utility model the first embodiment provides, this reality
Include boiler 1, condenser 2 and separate substance collector 4 with the separated device of the first new embodiment, wherein
The part connected between boiler 1 and condenser 2 is referred to as connecting portion 3.
The outside of boiler 1 is provided with water circle device, can ensure the temperature in boiler 1, and according to specific separation
The difference of material, the temperature of water is controlled, to meet the purpose of distillation.Thermometer can also be set in boiler 1, to monitor at any time
Temperature in boiler 1.It should be noted that the water circle device outside boiler 1 can enter the regulation of trip temperature, according to tool
The needs of body, set different water temperatures, without should narrow sense be considered hot water or circulating chilled water device.
The outside of condenser 2 is provided with water circle device (not shown), to ensure that steam enters in condenser 2, with
After the side wall 22 of condenser 2 contacts, because the temperature of side wall 22 is relatively low, steam can be condensed into liquid.Can be with condenser 2
Thermometer is set, to monitor the temperature in condenser 2 at any time.Equally, it should be noted that the water circulation dress outside condenser 2
The regulation of trip temperature can be entered by putting, and according to specific needs, set different water temperatures, without should narrow sense be considered hot water or
Person's circulating chilled water device.
Fig. 2 is the sectional view of condenser 2 in the condensing unit that the utility model the first embodiment provides, condenser 2
The spheroidal shape expanded with middle part, such design, the surface area of the side wall 22 of condenser 2 can be increased, make steaming
Vapour and the contact area of side wall 22 are bigger, so as to improve the efficiency of condensation.
In addition, as shown in Fig. 2 in the first embodiment of the present utility model, side wall 22 divide for upper portion side wall 221,
Lower sides 222 and upper portion side wall 221 and the pars intermedia side wall 223 of the junction of lower sides 222；In it should be noted that
Between portion's side wall 223 represents is place that upper portion side wall 221 is connected with lower sides 222, it is not carried out strict
Region division.
Upper portion side wall 221 is similar hemispheric curvilinear plane, and lower sides 222 are the planarea of similar taper, Er Qiezhong
Between the diameter of portion's side wall 223 be the maximum position of the whole diameter of condenser 2, such design, it is larger both to have ensure that side wall 22 had
Surface area, enable again condensation liquid along side wall 22 downstream to reservoir 23 in, and be unlikely to nature it is low to steam
Evaporate in pot 1.Moreover, it is a smooth face that side wall 22 is overall, without the stop of barrier, it more ensure that liquid can be smoothly
Downstream in reservoir 23.
In the first embodiment of the present utility model, the diameter of pars intermedia side wall 223 is the 2 of the diameter of connecting portion 3
Times.In addition, when 1.5-3 times of the diameter of a diameter of connecting portion 3 of pars intermedia side wall 223, it can all reach a preferably condensation
Effect, such as can be, but it is not limited to 1.5,2,2.5 or 3 times.
The bottom of condenser 2 sets the oriented inclined intercepter plate 21 in the side of condenser 2, the side wall 22 of condenser 2 and dams
Plate 21 forms reservoir 23, and reservoir 23 can be stored along the dirty liquid of the condensation of side wall 22.
Intercepter plate 21 is arranged at the bottom of condenser 2, and is tilted to the side of condenser 2, the He of side wall 22 of such condenser 2
Intercepter plate 21 will form the reservoir 23 of " V " type, after the gas of evaporation in boiler 1 enters condenser 2, due to side
The temperature of wall 22 is relatively low, and gas, which runs into side wall 22, can be condensed into liquid, and liquid can flow down along side wall 22, be blocked until being trapped plate 21
Cut, so as to collect in reservoir 23.
" V " type herein being related to, is only the description to the shape of reservoir 23, and not representing reservoir 23 has stricti jurise
On " V " word shape.For example, a kind of the improving as the first embodiment of the utility model, can also be by side wall 22 with cutting
The position that flowing plate 21 contacts is designed as the angle of arc, rather than proper " V " type angle, such design, gets rid of completely
Except the dead ends of cleanning of condenser 2, more fully condenser 2 can be cleared up.Certainly, even if reservoir 23 is strict meaning
" V " font in justice, the first embodiment technical problems to be solved of the utility model are similarly can solve the problem that, ensure distillation
The condensation effect of separator.
As shown in Fig. 2 in the first embodiment of the present utility model, the diameter of connecting portion 3 is the width of intercepter plate 21
5 times, such design, can ensure that steam can be rapidly entered in condenser 2, and be unlikely to be trapped plate 21 and intercept.In addition,
When the diameter of connecting portion 3 is 4-6 times of the width of intercepter plate 21, it can ensure that steam can be rapidly introduced into condenser 2
In, such as can be, but it is not limited to 4,4.5,5,5.5 or 6 times.
The top of condenser 2 is provided with open top 24, and steam can be allowed to be discharged to outside condenser 2, open top 24
Diameter is less than the diameter of connecting portion 3, to ensure that steam will not be discharged quickly from open top 24.In addition, as an improvement, may be used also
To connect a condensing unit at open top 24, the other end of condensing unit can be connected with boiler 1, and then form one
Individual circulation, to reduce the loss of material.
In the first embodiment of the present utility model, the diameter of connecting portion 3 is 3 times of the diameter of open top 24.Separately
Outside, when the diameter of connecting portion 3 is 2-4 times of the diameter of open top 24, a preferable condensation effect can all be reached, such as
It can be, but be not limited to 2,2.5,3,3.5 or 4 times.
In the first embodiment of the present utility model, in order that the liquid condensed in side wall 22 can be more
Enter reservoir 23 in, following Curve guide impeller can also be carried out：The width of Reasonable adjustment intercepter plate 21 and the angle with ground,
To cause side wall 22 and " V " the type reservoir 23 of the formation of intercepter plate 21, all sides in addition to open top 24 can be radiated
Wall 22.Such design, even if liquid can be ensured not along the following current of side wall 22, but naturally vertical drippage, it can also drip
Fall into reservoir 23, further increase the effect of condensation.
The ground herein being related to, refer to the ground of placement condensation separating unit.
The side of side wall 22 of reservoir 23 is further opened with liquid storage channel opening 25, and liquid storage channel opening 25 is connected with separate substance receipts
Storage 4, after condensed liquid enters reservoir 23, separate substance collector 4 can be flowed at liquid storage channel opening 25, so as to
Realize the collection to separate substance.
In addition, controlled valve is equipped with connecting portion 3, open top 24 and liquid storage channel opening 25, according to specific need
Ask, open or close the valve of relevant position, to increase the practicality of separated device.
Fig. 3 is the schematic diagram of boiler 1 in the condensing unit that the utility model the first embodiment provides, with reference to Fig. 1,
Fig. 2 and Fig. 3, exemplified by separating the substance A that boiling point is 80 DEG C and the substance B that boiling point is 70 DEG C, using of the present utility model the
During a kind of embodiment, A and B mixing liquid is added in boiler 1 by boiler charging aperture 11, the temperature of control boiler 1
Spend for 75 DEG C, liquid B can become steam B and enter in gaseous form in condenser 2, and liquid A can be retained in boiler 1
In.The temperature of the external water circulation device reclaimed water of condenser 2 is controlled below 70 DEG C, such as is controlled at 20 DEG C, steam B runs into temperature
The side wall 22 of low condenser 2, liquid B can be condensed into again, and be flow to along side wall 22 in reservoir 23, travel further into point
From in collecting material device 4.The bottom of separate substance collector 4 and boiler 1 is equipped with opening, after still-process terminates, beats
Open the opening of separate substance collector 4 and the bottom of boiler 1, collect respectively, that is, the liquid A and liquid B separated.
The first embodiment of the present utility model breaches the structure limitation of traditional condenser pipe, larger using surface area
The happening part that is condensed as steam of the spheroidal condenser 2 of class, it is real and by setting intercepter plate 21 in the bottom of condenser 2
The purpose of separated is showed.The separated device that the first embodiment of the utility model provides can either ensure distillation
Effectively carry out, provide new mentality of designing for distilling apparatus again.Moreover, condenser 2 does not have the dead ends of cleanning substantially, have easy
In cleaning the advantages of, when being particularly applied in food processing process, the complete monitoring to food processing process can be ensured.
Fig. 2 is the overall structure diagram for the white wine impurity removing equipment that second of embodiment of the utility model provides, including
Separated equipment in the first embodiment, the content being related in the first embodiment are here no longer described in detail.
In addition, the white wine impurity removing equipment that second of embodiment of the utility model provides is opened at the top of condenser 2
Clarifier 5 is also associated with mouth 24, the other end of clarifier 5 is also associated with condensing collector 6.
In second of embodiment of the present utility model, clarifier 5 is internally provided with acticarbon, can inhale
Take in the harmful substance in the gas of clarifier 5.
The white wine knot screen that second of embodiment of the utility model provides can remove the harmful substance in white wine,
In use, white wine is added in boiler 1 from boiler charging aperture 11, it is 70-75 DEG C to control the temperature in boiler 1, example
Such as 73 DEG C, and condenser 2 is controlled to be in relatively low temperature, such as 25 DEG C, now, white wine mid-boiling point is less than 73 DEG C of harmful substance
It can evaporate into condenser 2, harmful substance is condensed into liquid again in condenser 2, and enters separate substance collector 4
In；After harmful substance of the boiling point less than 73 DEG C is basically separated completely, the temperature in boiler 1 is controlled to be in 80-95 DEG C, example
Such as 90 DEG C, and the temperature in condenser 2 is controlled to be similarly in 90 DEG C, now, white wine mid-boiling point is higher than 90 DEG C of harmful substance meeting
Remain in boiler 1, and the active ingredient ethanol of white wine can as a vapor (will not be cold by condenser 2
It is solidifying), enter in clarifier 5, the acticarbon in clarifier 5 can adsorb the harmful substance in white wine steam, then, in vain
Wine steam is entered in condensing collector 6, is condensed into liquid again, that is, has obtained removing the white wine of harmful substance impurity.
As shown in figure 5, the improvement as clarifier 5, clarifier 5 may also include clarifier import 51, gaseous state is separated by filtration
Tower 53, the first condenser 54, the second condenser 55 and clarifier outlet 52, wherein clarifier import 51, gaseous state is separated by filtration tower
53rd, the first condenser 54, the second condenser 55 and clarifier outlet 52 are sequentially connected, and the top of the second condenser 55 is also associated with
Harmful substance condenser pipe 56, wherein gaseous state are separated by filtration in tower 53 and are provided with acticarbon.
After the purified device import 51 of white wine steam enters clarifier 5, gaseous state is separated by filtration the charcoal absorption in tower 53
Agent can remove the harmful substances such as methanol in wine, lead, plasticiser, sulphur, zinc, free radical, and white wine steam enters the first condensation immediately
Device 54, it is condensed into liquid and enters the second condenser 55, due to the gaseous impurities being not yet condensed inevitably be present, in order to
The part gaseous impurities is removed as far as possible, and harmful substance condenser pipe 56, gaseous state are also associated with the top of the second condenser 55
Harmful substance is separated after the condensation of harmful substance condenser pipe 56, further through the second condenser 55 by the white wine of separation, impurity removal
After condensation, it is connected by clarifier outlet 52 with condensing collector 6, collects and obtain the separated white wine of impurity.
In addition, gaseous state is separated by filtration in tower 53 also settable mineral material, it can equally play and good go the removal of impurity
Effect, it is and natural harmless.
The white wine impurity removing equipment that second of embodiment of the utility model provides, passes through provide the first embodiment
Separated device and clarifier 5 are combined with each other, and can either separate the relatively low harmful substance of boiling point, and and can enough separates boiling point
Higher harmful substance, while the harmful substance in white wine can also be further removed by purifier.By this second
White wine after the white wine impurity removing equipment processing that embodiment provides, the content of wherein harmful substance substantially reduce, obtained white wine
It is a kind of white wine of ecological safety health.
Finally it should be noted that：Various embodiments above is only to illustrate the technical solution of the utility model, rather than it is limited
System；Although the utility model is described in detail with reference to foregoing embodiments, one of ordinary skill in the art should
Understand：It can still modify to the technical scheme described in foregoing embodiments, either to which part or whole
Technical characteristic carries out equivalent substitution；And these modifications or replacement, the essence of appropriate technical solution is departed from this practicality newly
The scope of each embodiment technical scheme of type.
Claims (10)
1. a kind of separated device, it is characterised in that the separated device includes：
Boiler (1), and condenser (2) of the through connection above the boiler (1)；
The condenser (2) has the shape that middle part is expanded；
Condenser (2) bottom sets the inclined intercepter plate in oriented condenser (2) side (21), the condenser (2)
Side wall (22) and the intercepter plate (21) form reservoir (23), the reservoir (23) can be stored along the side wall
(22) the dirty liquid of condensation；
The reservoir (23) is circumscribed with separate substance collector (4).
2. separated device according to claim 1, it is characterised in that the top of the condenser (2) is provided with top
It is open (24), the diameter of the open top (24) is less than the connecting portion that the condenser (2) is connected with the boiler (1)
(3) diameter.
3. separated device according to claim 2, it is characterised in that the diameter of the open top (24) with it is described
The diameter proportion of connecting portion (3) is 1：2-4.
4. separated device according to claim 3, it is characterised in that the side wall (22) is included into the upper of curvilinear plane
Portion's side wall (221), the lower sides (222) in the face that is in line, and the upper portion side wall (221) and the lower sides (222)
The pars intermedia side wall (223) of junction；The pars intermedia side wall (223) is at the maximum gauge of the condenser (2).
5. separated device according to claim 4, it is characterised in that the diameter of the pars intermedia side wall (223) with
The diameter proportion of the connecting portion (3) is 1.5-3：1.
6. separated device according to claim 5, it is characterised in that the diameter of the pars intermedia side wall (223) with
The diameter proportion of the connecting portion (3) is 2：1.
7. separated device according to claim 2, it is characterised in that be provided with water outside the condenser (2) and follow
Loop device.
8. separated device according to claim 2, it is characterised in that be provided with water circulation outside the boiler (1)
Device.
9. a kind of white wine impurity removing equipment, it is characterised in that the white wine impurity removing equipment includes：Described in claim any one of 2-6
Separated device, the clarifier (5) being connected with the open top (24), and being connected with the clarifier (5) cold
Solidifying collector (6).
10. white wine impurity removing equipment according to claim 9, it is characterised in that be provided with activated carbon in the clarifier (5)
Adsorbent.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720401841.2U CN206666493U (en) | 2017-04-17 | 2017-04-17 | Separated device and apply its white wine impurity removing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720401841.2U CN206666493U (en) | 2017-04-17 | 2017-04-17 | Separated device and apply its white wine impurity removing equipment |
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| Publication Number | Publication Date |
|---|---|
| CN206666493U true CN206666493U (en) | 2017-11-24 |
Family
ID=60381830
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| Application Number | Title | Priority Date | Filing Date |
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| CN201720401841.2U Expired - Fee Related CN206666493U (en) | 2017-04-17 | 2017-04-17 | Separated device and apply its white wine impurity removing equipment |
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| CN (1) | CN206666493U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109182062A (en) * | 2018-11-09 | 2019-01-11 | 湖北工业大学 | It is a kind of for improving the purification medium and its purification method of Maotai-flavor former wine quality |
| CN112322442A (en) * | 2020-12-11 | 2021-02-05 | 钟春燕 | Method for preparing white spirit with improved fragrance |
| CN113373013A (en) * | 2020-07-01 | 2021-09-10 | 吉林奥真源酒业有限公司 | Ancient method distillation wine brewing device and technology |
-
2017
- 2017-04-17 CN CN201720401841.2U patent/CN206666493U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109182062A (en) * | 2018-11-09 | 2019-01-11 | 湖北工业大学 | It is a kind of for improving the purification medium and its purification method of Maotai-flavor former wine quality |
| CN113373013A (en) * | 2020-07-01 | 2021-09-10 | 吉林奥真源酒业有限公司 | Ancient method distillation wine brewing device and technology |
| CN112322442A (en) * | 2020-12-11 | 2021-02-05 | 钟春燕 | Method for preparing white spirit with improved fragrance |
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