CN207452062U - A kind of white liquor distilling does poor device - Google Patents

Abstract

The utility model provides a kind of white liquor distilling and does poor device, is related to brewed spirit field.White liquor distilling does poor device, including：Multiple dry poor towers being arranged in parallel, what each dry poor tower included being oppositely arranged loses poor import and loses poor outlet；Superheated steam manifold is respectively communicated with multiple dry poor towers and inputs superheated steam into multiple dry poor towers respectively in chronological order；Saturated vapor manifold is respectively communicated with multiple dry poor towers and is set away from superheated steam manifold.White liquor distilling does poor method and does poor device by using above-mentioned white liquor distilling to be dried to losing grain, and superheated steam is converted into saturated vapor in case recycling.

Description

A kind of white liquor distilling does poor device

Technical field

The utility model is related to brewed spirit fields, and poor device is done in particular to a kind of white liquor distilling.

Background technology

The distillation of white wine and steaming grain continue to use the traditional handicraft of more than one thousand years always, using saturated vapor as heat source；It makes Wine enterprise industry, which has, largely loses grain, and it is 60~65% to lose poor water content, and the drying means for losing grain is to be arrived first with squeezer extrusion dehydration Water content about 50~55%, reusable heat can be dried to after water content about 10% to do feed or fuel.

The shortcomings that distillation of white wine and steaming grain traditional handicraft：Saturated vapor is then condensed into water to the cold and forms residual water；This It is outer to also have the yellow water formed in fermentation vat, evaporate liquor tailing water after drinking；The bubble grain water of fen-flavor type white spirit, stewing grain water.Above-mentioned waste water is most For end form into sewerage, sewage quantity is 10 ton/ton white wine, it is necessary to by processing, could be discharged after reaching primary standard.

Liquor-making enterprise poor unstrained spirits of having more than needed forms after string steams and takes perfume (or spice) and loses grain, loses poor water content for 60~65%, unsuitable long-distance Transport, such as drying and dehydrating not in time, can rot smelly.The drying means for losing grain is first with squeezer extrusion dehydration to water content About 50~55%, reusable heat can be dried to after water content about 10% to do feed or fuel, and drying needs to consume a large amount of thermal energy.

In view of this, the utility model is proposed.

Utility model content

The purpose of this utility model is to provide a kind of white liquor distillings to do poor device, can use superheated steam to lose grain into Row is dry and generates saturated vapor.

The another object of the utility model is that providing a kind of white liquor distilling does poor method, have easy to operate and effect compared with The characteristics of good.

What the embodiment of the utility model was realized in：

The utility model provides a kind of white liquor distilling and does poor device, including：

Multiple dry poor towers being arranged in parallel, what each dry poor tower included being oppositely arranged loses poor import and loses poor outlet；

Superheated steam manifold is respectively communicated with multiple dry poor towers and was inputted respectively into multiple dry poor towers in chronological order Hot steam；

Saturated vapor manifold is respectively communicated with multiple dry poor towers and is set away from superheated steam manifold.

In the utility model preferred embodiment, above-mentioned dry poor tower includes cylinder tower body and the circle connected with cylinder tower body Tower body is bored, superheated steam manifold is connected with the end of the separate cylinder tower body of circular cone tower body, saturated vapor manifold and cylinder tower body Separate circular cone tower body end connection, lose the end that poor import is arranged at the separate circular cone tower body of cylinder tower body, lose poor outlet It is arranged at the end of the separate cylinder tower body of circular cone tower body.

In the utility model preferred embodiment, the outside that covers at circular cone tower body is further included and between circular cone tower body The first tower lid of inlet chamber is formed, circular cone tower body is provided with the venthole of the inner cavity of connection inlet chamber and dry poor tower, loses poor outlet It stretches out outside the first tower lid, superheated steam manifold is connected with inlet chamber.

In the utility model preferred embodiment, above-mentioned first tower lid, which is additionally provided with to close, loses the first of grain outlet Sealing cover, the first sealing cover include the first mounting base, the first material mouth lid and are pivotally connected with the first mounting base and the first material mouth lid The first pivoted pole, the first mounting base is arranged at the first tower lid, and the first material mouth lid is detachably connected with losing grain outlet.

In the utility model preferred embodiment, above-mentioned superheated steam manifold includes the first steam pipe, air inlet pipe and mistake Hot steam inlet valve, the first steam pipe are connected with multiple dry poor towers, and air inlet pipe connects with the first steam pipe and is used to steam to first Input superheated steam, the close end set connected with each air cavity of the first steam pipe have superheated steam inlet valve in steam pipe.

In the utility model preferred embodiment, the second tower lid for being arranged at cylinder tower body is further included, poor import is lost and sets Be placed in the second tower lid, the second tower lid is additionally provided with thermocouple and relief valve, the connection of the second tower of saturated steam pipe lid and with dry poor tower Inner cavity connection.

In the utility model preferred embodiment, above-mentioned second tower lid is additionally provided with loses the second of poor import for closing Sealing cover, the second sealing cover include the second mounting base, the second material mouth lid and are pivotally connected with the second mounting base and the second material mouth lid The second pivoted pole, the second mounting base is arranged at the second tower lid, and the second material mouth lid is detachably connected with losing poor import.

In the utility model preferred embodiment, above-mentioned saturated vapor manifold includes the second steam pipe, air outlet pipe and satisfies And steam outlet valve, the second steam pipe are connected with multiple dry poor towers, air outlet pipe connects with the second steam pipe and is used to steam second Saturated vapor discharge in steam pipe, the close end set connected with each dry poor tower of the second steam pipe have saturated vapor outlet Valve.

In the utility model preferred embodiment, above-mentioned second tower lid is directed away from the direction protrusion of circular cone tower body.

In the utility model preferred embodiment, further include and be arranged at dry poor tower and lose poor object for detecting in dry poor tower The level detector of the height change of material.

The advantageous effect of the utility model embodiment is：

The white liquor distilling of the utility model embodiment does poor device, is dried and is converted into losing grain using superheated steam On the one hand saturated vapor obtains dry grain of losing, on the other hand, the total enthalpy of superheated steam to saturated vapor does not become Change, subsequent applied to wine brewing process evaporates wine and steaming grain.Have the characteristics that energy saving and reduce cost.

Description of the drawings

It, below will be to required use in embodiment in order to illustrate more clearly of the technical solution of the utility model embodiment Attached drawing be briefly described, it should be understood that the following drawings illustrates only some embodiments of the utility model, therefore should not be by Regard the restriction to scope as, for those of ordinary skill in the art, without creative efforts, may be used also To obtain other relevant attached drawings according to these attached drawings.

Fig. 1 is the structure diagram at the first visual angle that the white liquor distilling that the utility model embodiment provides does poor device；

Fig. 2 be II in the Fig. 1 provided at close-up schematic view；

Fig. 3 be III in the Fig. 1 provided at close-up schematic view；

Fig. 4 is the schematic diagram for the circular cone tower body that the utility model embodiment provides.

Icon：100- white liquor distillings do poor device；110- does poor tower；111- cylinder tower bodies；112- circular cone tower bodies；1121- Venthole；1122- discharge ports；113- level detectors；120- the second tower lids；121- the second lid bodies；122- loses poor import；123- Two sealing covers；The second mounting bases of 1231-；The second pivoted poles of 1232-；1233- the second material mouth lids；124- thermocouples；125- pressure releases Valve；130- the first tower lids；131- air cavitys；132- loses poor outlet；The first sealing covers of 133-；The first mounting bases of 1331-；1332- One pivoted pole；1333- the first material mouth lids；140- superheated steams manifold；The first steam pipes of 141-；142- air inlet pipe；143- is overheated Steam inlet valve；150- saturated vapors manifold；The second steam pipes of 151-；152- air outlet pipes；153- saturated vapor outlet valves.

Specific embodiment

It is new below in conjunction with this practicality to make the purpose, technical scheme and advantage of the utility model embodiment clearer Attached drawing in type embodiment, the technical scheme in the utility model embodiment is clearly and completely described, it is clear that is retouched The embodiment stated is the utility model part of the embodiment, instead of all the embodiments.Usually here described in attached drawing and The component of the utility model embodiment shown can configure to arrange and design with a variety of.

Therefore, requirement is not intended to limit to the detailed description of the embodiment of the utility model provided in the accompanying drawings below The scope of the utility model of protection, but it is merely representative of the selected embodiment of the utility model.Based in the utility model Embodiment, those of ordinary skill in the art's all other embodiments obtained without creative efforts, all Belong to the scope of the utility model protection.

It should be noted that：Similar label and letter represents similar terms in following attached drawing, therefore, once a certain Xiang Yi It is defined, then it further need not be defined and explained in subsequent attached drawing in a attached drawing.

, it is necessary to explanation, the instructions such as term " on ", " under ", " interior ", " outer " in the description of the utility model embodiment Orientation or position relationship be usual when being used based on orientation shown in the drawings or position relationship or the utility model product The orientation or position relationship put are for only for ease of description the utility model and simplify description rather than instruction or imply institute The device or element of finger must have specific orientation, with specific azimuth configuration and operation, therefore it is not intended that this reality With new limitation.In addition, term " first ", " second " etc. are only used for distinguishing description, and it is not intended that instruction or hint phase To importance.

In the description of the utility model embodiment, it is also necessary to explanation, unless otherwise clearly defined and limited, art Language " setting ", " installation ", " connected ", " connection " should be interpreted broadly, for example, it may be being fixedly connected or detachably Connection is integrally connected；Can be mechanical connection or electrical connection；It can be directly connected, centre can also be passed through Medium is indirectly connected, and can be the connection inside two elements.It for the ordinary skill in the art, can specific feelings Condition understands concrete meaning of the above-mentioned term in the utility model.

Refer to Fig. 1, white liquor distilling does poor device 100, including dry poor tower 110, the second tower lid 120, the first tower lid 130, Superheated steam manifold 140 and saturated vapor manifold 150.Wherein, the opposite end for doing poor tower 110 is respectively arranged with the second tower lid 120 and the first tower lid 130.Superheated steam manifold 140 is connected by the first tower lid 130 with the inner cavity of dry poor tower 110；Saturated vapor Manifold 150 is connected by the second tower lid 120 with the inner cavity of dry poor tower 110.

Wherein, it is multiple to do being provided with for poor 110 parallel connection of tower, in the present embodiment exemplified by setting two, setting three, four A or more dry poor 110 situation of tower is similar with setting the situation of two, and therefore not to repeat here.

Fig. 1 and Fig. 4 are refer to, doing grain tower 110 includes cylinder tower body 111 and circular cone tower body 112.Cylinder tower body 111 and circle Bore tower body 112.Cylinder tower body 111 has first inner chamber (figure does not mark), and circular cone tower body 112 has second inner chamber, and (figure is not marked Note).Cylinder tower body 111 and circular cone tower body 112 connect so that first inner chamber is connected with second inner chamber forms dry poor tower 110 Inner cavity.

It is appreciated that when dry grain tower 110 is vertically arranged, the end of the separate circular cone tower body 112 of cylinder tower body 111 is dry grain The upper end of tower 110, and the opening that the end has is for launching the import for losing grain；The separate cylinder tower body of circular cone tower body 112 111 end is the lower end of dry poor tower 110, and the opening that the end has is for discharging the outlet for losing grain.

Further, the opening of cylinder tower body 111 is feed inlet (figure does not mark)；The opening of circular cone tower body 112 is Discharge port 1122.

The end set of the separate circular cone tower body 112 of cylinder tower body 111 has level detector 113.Specifically, level detector 113 is set It is placed in the end of its close feed inlet of cylinder tower body 111.Level detector 113 is used to detect the height for losing poor material in dry poor tower 110 Degree variation.

Fig. 1 and Fig. 3 are refer to, the first tower lid 130 covers at the outer wall of circular cone tower body 112.It is appreciated that the first tower lid 130 shape and structure is similar with the shape and structure of circular cone tower body 112.

Form air cavity 131 between the inner wall of first tower lid 130 and the outer wall of circular cone tower body 112, circular cone tower body 112 by the The part that one tower lid 130 is provide with is provided with multiple ventholes 1121.By multiple ventholes 1121, by air cavity 131 and dry poor tower 110 inner cavity connection.

Preferably, venthole 1121 have in circular cone tower body 112 close to the end set for losing grain outlet 132 it is multiple.

First tower lid 130, which is provided with, loses grain outlet 132, loses grain outlet 132 and stretches out the first tower lid 130 away from cylinder tower body 111 outside.When first tower lid 130 is provide with circular cone tower body 112, discharge port 1122 is connected with losing grain outlet 132, and for inciting somebody to action The dry poor tower 110 of grain discharge is lost in dry grain tower 110.

First tower lid 130 is provided with to close and open the first sealing cover 133 for losing grain outlet 132.First sealing cover 133 include the first mounting base 1331, the first pivoted pole 1332 and the first material mouth lid 1333.

Specifically, the first mounting base 1331 is arranged at the outer wall of the first tower lid 130 and is directed away from the side of cylinder tower body 111 To stretching, the both ends of the first pivoted pole 1332 are pivotally connected respectively with the first mounting base 1331 and the first material mouth lid 1333, the first pivot joint The the first material mouth lid 1333 of drive of bar 1332, which can be closed or opened, loses grain outlet 132.That is, first material mouth lid 1333 with losing poor outlet 132 are detachably connected.

Fig. 1 and Fig. 3 are continued referring to, superheated steam manifold 140 includes the first steam pipe 141, air inlet pipe 142 and overheat and steams Vapour inlet valve 143.

Specifically, the both ends of the first steam pipe 141 and the air cavity 131 of two dry poor towers 110 are respectively communicated with, air inlet pipe 142 It is connected with the first steam pipe 141 and for inputting superheated steam into the first steam pipe 141, it will be understood that the first steam pipe 141 The separate end connected with the first steam pipe 141 for being connected with source of the gas.

The close end set connected with each air cavity 131 of first steam pipe 141 has superheated steam inlet valve 143.It can To understand, superheated steam inlet valve 143 is identical with the number of dry poor tower 110, and for the first steam pipe 141 of control opening or It closes.

Hold above-mentioned, superheated steam is respectively enterd by the first steam pipe 141 in two dry poor towers 110, and is passed through overheat and steamed The opening at the both ends interval of 143 the first steam pipe of Separation control 141 of vapour inlet valve realizes being done to two liang in poor towers 110 for interval Input superheated steam is used for the drying to losing grain.

Referring to Fig.1 and 2, the second tower lid 120 covers at cylinder tower body 111 and closes feed inlet.

Second tower lid 120 includes the second lid body 121.Second lid body 121 is the shape similar to pot cover, towards far Direction protrusion from circular cone tower body 112.It sets in this way so that there is a fixed gap between feed inlet and the second tower lid 120 For buffering, discharge drying is contributed to lose grain and obtains saturated vapor.

Second lid body 121, which is provided with, loses poor import 122.Lose the separate conical tower that the second tower lid 120 is stretched out in poor import 122 The outside of body 112.When second tower lid 120 is provide with cylinder tower body 111, by losing input of the poor import 122 into dry poor tower 110 Lose grain.

Second tower lid 120 is provided with to close and open the second sealing cover 123 for losing poor import 122.Second sealing cover 123 include the second mounting base 1231, the second pivoted pole 1232 and the second material mouth lid 1233.

Specifically, the second mounting base 1231 is arranged at the outer wall of the second tower lid 120 and is directed away from the side of circular cone tower body 112 To stretching, the both ends of the second pivoted pole 1232 are pivotally connected respectively with the second mounting base 1231 and the second material mouth lid 1233, the second pivot joint The the second material mouth lid 1233 of drive of bar 1232, which can be closed or opened, loses poor import 122.That is, second material mouth lid 1233 with losing poor import 122 are detachably connected.

Second tower lid 120 is additionally provided with thermocouple 124 and relief valve 125.Wherein, thermocouple 124 is lost for measuring to flow through The temperature of the superheated steam of grain, is saturated vapor when its temperature reaches particular value, opens relief valve 125 and passes through saturated vapor Saturated vapor manifold 150 is discharged.

It is appreciated that superheated steam flow through in dry poor tower 110 lose grain after, be converted into saturated vapor.

Fig. 1 and Fig. 2 are continued referring to, saturated vapor manifold 150 includes the second steam pipe 151, air outlet pipe 152 and saturation and steams Vapor outlet valve 153.

Specifically, the both ends of the second steam pipe 151 are connected respectively by the inner cavity of the second tower lid 120 and two dry poor towers 110 Logical, air outlet pipe 152 connects with the second steam pipe 151 and for the saturated vapor in the second steam pipe 151 to be discharged, discharge Saturated vapor can be used for wine brewing process it is follow-up evaporate wine and steam grain.

The close end set connected with each inner cavity of second steam pipe 151 has saturated vapor outlet valve 153.It can manage Solution, saturated vapor outlet valve 153 is identical with the number of dry poor tower 110, and plays on or off for the second steam pipe 151 of control It closes.

Hold above-mentioned, saturated vapor is discharged by the second steam pipe 151 respectively outside two dry poor towers 110, and is passed through saturation and steamed The opening at the both ends interval of 153 the first steam pipe of Separation control 141 of vapor outlet valve realizes being done to two liang outside poor towers 110 for interval Discharge.

Second tower lid 120, cylinder tower body 111,112 and first tower lid 130 of circular cone tower body are set gradually, also, lose grain into Mouth 122 is oppositely arranged with grain outlet 132 is lost, and loses the end that poor import 122 is arranged at the separate circular cone tower body 112 of cylinder tower body 111 Portion loses the end that grain outlet 132 is arranged at the separate cylinder tower body 111 of circular cone tower body 112；Superheated steam manifold 140 and circular cone The end connection of the separate cylinder tower body 111 of tower body 112, the separate circular cone tower body of saturated vapor manifold 150 and cylinder tower body 111 112 end connection.

A kind of white liquor distilling that poor device 100 is done using above-mentioned white liquor distilling does poor method, including：

Grain is lost by losing poor import 122 and being separately added into each dry poor tower 110, is lost by the closing of the second sealing cover 123 Poor import 122.At this point, grain outlet 132 is lost in the closing of the first sealing cover 133.

In order to improve drying efficiency, in each dry poor tower 110, equal filler, which loses grain to 113 position of level detector, is advisable.

It is realized by the opening and closing successively for controlling two superheated steam inlet valves 143 in parallel through hot steam manifold 140 intervals input superheated steam into two dry poor towers 110 successively.The index of superheated steam is：Pressure is 0.5~0.8MPa It it is 400~500 DEG C with temperature.

It is appreciated that in two superheated steam inlet valves 143, one when opening, another closing.Realize two it is in parallel Dry grain tower 110 is used alternatingly, and ensures white liquor distilling drying device persistently to losing grain drying and continuously generating saturated vapor.That is, It is respectively communicated with two dry poor towers 110 and inputs superheated steam into two dry poor towers 110 respectively in chronological order.

Superheated steam flows through lose grain after be converted into saturated vapor.It is detected by thermocouple 124 and flows through the superheated steam for losing grain Pressure be 0.49~0.5MPa and when temperature is 146~156 DEG C, be above-mentioned saturated vapor.Relief valve 125 is opened, it will be full It is discharged with steam by saturated vapor manifold 150 in dry poor tower 110.

The first sealing cover 133 is opened, by dried grain of losing via losing the 132 dry poor tower 110 of discharge of grain outlet.

It holds above-mentioned, on the one hand, it is dried to lose grain, convenient for later use；On the other hand, superheated steam absorption is lost in grain Moisture content and reduce temperature so as to be converted into saturated vapor, and evaporate wine applied to the subsequent of wine brewing process and steam grain, meanwhile, saturation The lingering fragrance that grain is lost in steam carrying seals in wine body in subsequently using journey, plays the role of flavour passage.

In conclusion the white liquor distilling of the utility model embodiment does poor device 100, using superheated steam to losing poor progress It dries and is converted into saturated vapor, on the one hand obtain dry grain of losing, on the other hand, the total enthalpy of superheated steam to saturated vapor It does not change, subsequent applied to wine brewing process evaporates wine and steaming grain.Have the characteristics that energy saving and reduce cost.

The white liquor distilling of the utility model embodiment does poor method, on the one hand, and it is dried to lose grain, convenient for later use； On the other hand, superheated steam absorption loses the moisture content in grain and reduces temperature so as to be converted into saturated vapor, and is applied to make wine The subsequent of journey evaporates wine and steams grain, meanwhile, the lingering fragrance that grain is lost in saturated vapor carrying seals in wine body during follow-up use, plays The effect of flavour passage.Have the characteristics that easy to operate and effect is preferable.

The above is only the preferred embodiment of the utility model only, is not intended to limit the utility model, for this For the technical staff in field, various modifications and changes may be made to the present invention.It is all in the spirit and principles of the utility model Within, any modifications, equivalent replacements and improvements are made should be included within the scope of protection of this utility model.

Claims (10)

1. a kind of white liquor distilling does poor device, which is characterized in that including：

Multiple dry poor towers being arranged in parallel, what each dry poor tower included being oppositely arranged loses poor import and loses poor outlet；

Superheated steam manifold is respectively communicated with and defeated into multiple dry poor towers respectively in chronological order with multiple dry poor towers Enter superheated steam；

Saturated vapor manifold is respectively communicated with multiple dry poor towers and is set away from the superheated steam manifold.

2. white liquor distilling according to claim 1 does poor device, which is characterized in that the dry poor tower include cylinder tower body and The circular cone tower body connected with the cylinder tower body, the superheated steam manifold is with the circular cone tower body away from the cylinder tower body End connection, the end of the separate circular cone tower body of the saturated vapor manifold and the cylinder tower body connects, described to lose Poor import is arranged at the end away from the circular cone tower body of the cylinder tower body, and the grain outlet of losing is arranged at the conical tower The end away from the cylinder tower body of body.

3. white liquor distilling according to claim 2 does poor device, which is characterized in that further includes and covers at the circular cone tower body Outside and the first tower lid of inlet chamber is formed between the circular cone tower body, the circular cone tower body is provided with the connection air inlet The venthole of the inner cavity of chamber and the dry poor tower, the grain outlet of losing are stretched out outside the first tower lid, the superheated steam manifold It is connected with the inlet chamber.

4. white liquor distilling according to claim 3 does poor device, which is characterized in that the first tower lid, which is additionally provided with, to be used for Lost described in closing grain outlet the first sealing cover, first sealing cover include the first mounting base, the first material mouth lid and with institute It states the first mounting base and the first pivoted pole that the first material mouth lid is pivotally connected, first mounting base is arranged at the first tower lid, The first material mouth lid is detachably connected with the grain outlet of losing.

5. white liquor distilling according to claim 3 does poor device, which is characterized in that the superheated steam manifold includes first Steam pipe, air inlet pipe and superheated steam inlet valve, first steam pipe connects with multiple dry poor towers, the air inlet pipe and First steam pipe connects and is used into first steam pipe input superheated steam, first steam pipe it is close with The end set of each air cavity connection has superheated steam inlet valve.

6. white liquor distilling according to claim 2 does poor device, which is characterized in that further includes and is arranged at the cylinder tower body The second tower lid, described to lose poor import and be arranged at the second tower lid, the second tower lid is additionally provided with thermocouple and relief valve, Second tower lid connection described in the saturated steam pipe is simultaneously connected with the inner cavity of the dry poor tower.

7. white liquor distilling according to claim 6 does poor device, which is characterized in that the second tower lid, which is additionally provided with, to be used for Lose the second sealing cover of poor import described in closing, second sealing cover include the second mounting base, the second material mouth lid and with institute It states the second mounting base and the second pivoted pole that the second material mouth lid is pivotally connected, second mounting base is arranged at the second tower lid, The second material mouth lid is lost poor import and is detachably connected with described.

8. white liquor distilling according to claim 6 does poor device, which is characterized in that the saturated vapor manifold includes second Steam pipe, air outlet pipe and saturated vapor outlet valve, second steam pipe connects with multiple dry poor towers, the air outlet pipe and Second steam pipe connect and be used for by second steam pipe saturated vapor discharge, second steam pipe it is close The end set connected with each dry poor tower has saturated vapor outlet valve.

9. white liquor distilling according to claim 6 does poor device, which is characterized in that the second tower lid is directed away from described The direction protrusion of circular cone tower body.

10. poor device is done according to claim 1~9 any one of them white liquor distilling, which is characterized in that further include and be arranged at institute State dry poor tower and the level detector for detecting the height change that poor material is lost in the dry poor tower.