CN207899513U - A kind of wet disintegrating apparatus - Google Patents

Abstract

A kind of wet disintegrating apparatus provided by the utility model includes Roughpulverizer and slimer, the Roughpulverizer connection conveying equipment and the slimer, the dry grain of rice and hot water are mixed into the Roughpulverizer, it is able to carry out preliminary crushing to the grain of rice, wherein, the Roughpulverizer includes connections storehouse, guiding piece and a pair of rolls last item, the guiding piece is rotationally arranged between the connections storehouse and the roll-in axis, the connections storehouse is connected to conveying equipment, the periphery compartment of terrain of the guiding piece is equipped with radially projecting, it is able to guide the grain of rice between the roll-in axis by rotation, the Roughpulverizer is equipped with water inlet, it is able to mix the grain of rice and hot water in the Roughpulverizer.To make the grain of rice directly be crushed in water, operation is more convenient so that the grain of rice in Rice ＆ peanut milk is mixedly more uniform with water, increases grain of rice soaking effect, reduces soaking time.

Description

A kind of wet disintegrating apparatus

Technical field

The utility model is related to pure mellow wines to make field, specifically, being a kind of wet disintegrating apparatus prepared suitable for pure mellow wine.

Background technology

Pure mellow wine is using rice as primary raw material, and female by koji-making, alcoholic, the processes such as fermentation, storage brewing are prepared, and spend Number is generally at 13~15 degree or so, and wine and women-sensual pursuits is transparent, and taste has sweet, Xin Zhifen.

Traditional pure mellow wine preparation method includes washing a meter rice steeping, steamed rice cooling, raw material proportioning and feeding intake, ferment, storing brewing And etc..Wherein, it refers to agitation conveying rice to wash a meter rice steeping, is cooked, is spread out with meal braizing machine by rice in steep diel, then by rice Cool cooling.Rice and water are delivered in tank body, repeatedly put into distiller's yeast, then are fermented, store brewing.It is gelatinized liquefaction step more Complexity, rice need to put into larger manpower and place construction, increase the manufacturing cost of pure mellow wine, be unfavorable for from the grain of rice as Rice ＆ peanut milk Large-scale production so that domestic pure mellow wine prepares less, and the preparation process of domestic pure mellow wine is not perfect.Rice is gelatinized liquefied mode Still rice steeping, steamed rice in adhering to old ways always, cooling, brewing are less efficient.

Utility model content

The main purpose of the utility model is to provide a kind of wet disintegrating apparatus, overcome the deficiencies in the prior art makes The grain of rice directly crushes in water, and operation is more convenient so that the grain of rice in Rice ＆ peanut milk is mixedly more uniform with water, increases rice Grain soaking effect, reduces soaking time.

To achieve the above objectives, the technical solution adopted in the utility model is：A kind of wet disintegrating apparatus includes Roughpulverizer And slimer, the Roughpulverizer are connected to conveying equipment and the slimer, the dry grain of rice and hot water are mixed into described thick In pulverizer, it is able to carry out preliminary crushing to the grain of rice, wherein the Roughpulverizer includes connections storehouse, guiding piece and a pair of rolls Last item, the guiding piece are rotationally arranged between the connections storehouse and the roll-in axis, and the connections storehouse connection conveying is set Standby, the periphery compartment of terrain of the guiding piece is equipped with radially projecting, is able to guide the grain of rice between the roll-in axis by rotation, The Roughpulverizer is equipped with water inlet, is able to mix the grain of rice and hot water in the Roughpulverizer.

An embodiment according to the present utility model, the wet disintegrating apparatus further comprise shurry pump and pneumatic butterfly of sizing mixing Valve, the shurry pump are respectively arranged in the Roughpulverizer and the slimer, and the Pneumatic butterfly valve of sizing mixing is separately connected The Roughpulverizer and the slimer are able to pneumatically adjust the thick disintegrating machine and the slimer.

An embodiment according to the present utility model, the Roughpulverizer are equipped with hole of sizing mixing, and the hole of sizing mixing is set to described The lower section of roll-in axis, the Pneumatic butterfly valve of sizing mixing described in the connection of hole of sizing mixing.

An embodiment according to the present utility model, the Roughpulverizer further comprise level sensor and level sensing Device, the level sensor are connected to the connections storehouse, are able to detect the controlling level of the connections storehouse, the liquid level sensor connects The lower part for leading to the Roughpulverizer, is able to detect the liquid level of the Roughpulverizer.

An embodiment according to the present utility model, the slimer be equipped with cavity, first charging aperture, second charging aperture, First discharge port, the second discharge port and filter plate, the cavity are equipped with chamber fine crushing and filter chamber, and the filter plate separates institute It states cavity and forms the chamber fine crushing and the filter chamber, the first charging aperture and be located at the second charging aperture described Both sides at the top of slimer, first discharge port are connected to the filter chamber and the external world, the second discharge port lateral communication The chamber fine crushing and the external world, the first charging aperture are connected to the Roughpulverizer and the slimer, by described first into Material mouth, which is able to the unpolished rice of Roughpulverizer slurry being delivered to the slimer, to be crushed, the second charging aperture and described Second discharge port is connected.

An embodiment according to the present utility model, the slimer include decelerating motor, drive shaft, stirring parts and thin Broken axis, the decelerating motor connect the drive shaft, and the drive shaft is rotationally horizontally set at the top of the chamber fine crushing, The stirring parts are vertically connected to the both sides of the drive shaft respectively, and the axis fine crushing is set to the lower section of the stirring parts, institute State the gap that the gap between axis fine crushing is less than the roll-in axis in the Roughpulverizer.

An embodiment according to the present utility model, the stirring parts are equipped with stirring blade, and the stirring blade is from the drive Moving axis is evenly spaced apart to extend radially outwardly.

An embodiment according to the present utility model, the stirring blade are warp architecture, the stirring of each stirring parts Blade has 3.

An embodiment according to the present utility model, the inclined directions of two stirring parts is on the contrary, one tilts upward, and one A inclination is downward.

An embodiment according to the present utility model, the axis fine crushing are tooth type structures, and unpolished rice slurry gets enter into described fine crushing In gap between axis.

Description of the drawings

Fig. 1 is the schematic diagram of the pure mellow wine preparation system of a preferred embodiment according to the present utility model.

Fig. 2 is the module diagram of the pure mellow wine preparation system of above preferred embodiment according to the present utility model.

Fig. 3 is the schematic diagram of the grain of rice crushing system of above preferred embodiment according to the present utility model.

Fig. 4 is the schematic diagram of the wet disintegrating apparatus of above preferred embodiment according to the present utility model.

Fig. 5 is the schematic diagram of the slimer of above preferred embodiment according to the present utility model.

Fig. 6 is the structural perspective of the stirring blade of above preferred embodiment according to the present utility model.

Fig. 7 is the structural schematic diagram of the gelatinization liquefied pot of above preferred embodiment according to the present utility model.

Fig. 8 is the structural schematic diagram in the upper puddling portion of above preferred embodiment according to the present utility model.

Fig. 9 is the schematic diagram of the filtration system of above preferred embodiment according to the present utility model.

Figure 10 is the structural schematic diagram of the pre-filtrating equipment of above preferred embodiment according to the present utility model.

Figure 11 is the structural schematic diagram of the vertical blade filter of above preferred embodiment according to the present utility model.

Specific implementation mode

It is described below for disclosing the utility model so that those skilled in the art can realize the utility model.It retouches below Preferred embodiment in stating is only used as illustrating, it may occur to persons skilled in the art that other obvious modifications.

As shown in Figure 1 to 11 is a kind of pure mellow wine preparation system 1, and the pure mellow wine preparation system 1 includes rice crushing system 10, it is gelatinized before liquefied pot 20, fermentation system 40 after system 30 and fermentation, the rice crushing system 10 is for by the rice in water Grain is ground into Rice ＆ peanut milk material, and the gelatinization liquefied pot 20 is connected to system 30 before the rice crushing system 10 and fermentation, the dextrin Change tank 20 to be able to for Rice ＆ peanut milk material to be gelatinized liquefaction in Multi-stage stirring, generate liquefaction feed liquid, system 30 includes mixing before the fermentation Tank 32, distiller's yeast tank 33 and fermentation tank 35, the blending tank 32 is connected to the gelatinization liquefied pot 20 and the distiller's yeast tank 33, described Mixing of the distiller's yeast in the blending tank 32 being gelatinized in the liquefaction feed liquid and the distiller's yeast tank 33 in liquefied pot 20, the fermentation Tank 35 is connected to system 40 after the blending tank 32 and the fermentation, system 40 is prepared for pure mellow wine after the fermentation pan-fried wine, Store up wine, filtering and sterilization process.

System 30 further comprises lactic acid bacteria tank 31 and tubular heat exchanger 34, the lactic acid bacteria tank 31 before the fermentation It is respectively communicated with the gelatinization liquefied pot 20 and the blending tank 32, is able to adjust the gelatinization liquefied pot 20 and the mixing respectively The pH value of tank 32 is equipped with the tubular heat exchanger 34, is able to institute between the gelatinization liquefied pot 20 and the blending tank 32 The liquefaction feed liquid cooling of gelatinization liquefied pot 20 is stated, then is delivered in the blending tank 32, the blending tank 32 and the fermentation tank It is equipped with the tubular heat exchanger 34 between 35, is able to the feed liquid cooling of the blending tank 32 being delivered to the fermentation tank 35 In, then ferment.

System 40 includes decocting wine system 43, wine storage tank 44, filtration system 47 and disinfection system 48 after the fermentation, described It decocts wine system 43 and is connected to the fermentation tank 35, the wine storage tank 44 is connected to the pan-fried wine system 43, is able to stand storage wine liquid, institute It states filtration system 47 to be set between the wine storage tank 44 and the disinfection system 48,47 multistage filtering wine of the filtration system Liquid, the disinfection system 48 extend the shelf-life of pure mellow wine for sterilizing to wine liquid.

Wherein, system 40 further comprises centrifuge 41, settling tank 42, plate heat exchanger 45 and freezing after the fermentation Tank 46 is blent, the centrifuge 41 is connected to the fermentation tank 35 and the settling tank 42, the wine filtered by the centrifuge 41 Liquid is stood into the settling tank 42, and convenient for extraction supernatant wine liquid, the settling tank 42 is connected to the pan-fried wine system 43, the plate Formula heat exchanger 45 is connected to the wine storage tank 44 and tank 46 is blent in the freezing, is able to the storage by the plate heat exchanger 45 The wine liquid of wine tank 44 cools down, then is delivered to the freezing and blends tank 46, carries out freezing and blends, the filtration system 47 is connected to described Tank 46 is blent in freezing.

The grain of rice crushing system 10 includes wet disintegrating apparatus 11, cleaner 12 and conveying equipment 14, the dedusting Equipment 12 is connected to the conveying equipment 14, and the conveying equipment 14 is connected to the wet disintegrating apparatus 11, and the cleaner 12 obtains To absorb the suspended state particle generated in the conveying equipment 14, the conveying equipment 14 is for the conveying grain of rice and removal rice Impurity in grain, improves the precision of the grain of rice, is interfered to prevent causing to crush to the wet disintegrating apparatus 11.

The wet disintegrating apparatus 11 includes Roughpulverizer 18 and slimer 19, and the Roughpulverizer 18 is connected to described defeated It send equipment 14 and the slimer 19, the dry grain of rice and hot water to be mixed into the Roughpulverizer 18, is able to carry out just the grain of rice Step crushes, and the slimer 19 is connected to the Roughpulverizer 18 and the gelatinization liquefied pot 20, the slimer 19 with Rice ＆ peanut milk material of milling is refined in further, improves the mixability of the grain of rice and water, improves Rice ＆ peanut milk material in the gelatinization liquefied pot 20 Liquefaction feed liquid quality, improve and be gelatinized liquefied efficiency, the grain of rice is made to become sufficiently starch granules, improve conversion effect.

The gelatinization liquefied pot 20 is equipped with driving motor 21, rotation axis 22, steam jacket 23 and agitating device 25, described Driving motor 21 connects the rotation axis 22, and the rotation axis 22 is vertically arranged in the gelatinization liquefied pot 20, the stirring 25 compartment of terrain of device is connected to the rotation axis 22, is able to rotate, the steam jacket with the rotation of the rotation axis 22 23 are coated on the outside of the gelatinization liquefied pot 20, are able to carry out steam heating to the gelatinization liquefied pot 20.It is steamed to pass through The heating power of vapour obtains so that starchiness expansion makes the grain of rice be gelatinized in Rice ＆ peanut milk.

Wherein, the agitating device 25 includes upper puddling portion 251 and lower puddling portion 252, the upper puddling portion 251 and institute The both sides up and down that lower 252 compartment of terrain of puddling portion is installed on the rotation axis 22 are stated, described in the upper puddling portion 251 is flatly stirred The lower part in the gelatinization liquefied pot 20 is obliquely stirred in the top Rice ＆ peanut milk material being gelatinized in liquefied pot 20, the lower puddling portion 250 Rice ＆ peanut milk material, contribute to increase Rice ＆ peanut milk material circulation rate, reduce Rice ＆ peanut milk material it is described gelatinization liquefied pot 20 in delay, reflux and Dead zone effectively reduces deposition, improves conversion ratio of the Rice ＆ peanut milk material to starch granules, while it is unidirectional to avoid single agitating device from being formed Whirlpool causes part Rice ＆ peanut milk material that can not be converted into effective starch granules.

Wherein, the upper puddling portion 251 is able to horizontal shear stirring Rice ＆ peanut milk material, and the upper puddling portion 251 is equipped with an installation Hole 254 and a plurality of upper puddling hole 255, the mounting hole 254 are opened in the center in the upper puddling portion 251, the upper puddling 255 compartment of terrain bar shaped of hole is opened in the both sides in the upper puddling portion 251, and the width in the upper puddling hole 255 is gradual from inside to outside Increase, be conducive to the axial flowing for enhancing Rice ＆ peanut milk material, balance top rice pulp flow state is convenient for 252 meters of the lower puddling portion The stirring of slurry so that Rice ＆ peanut milk material is in strong turbulence state, prevents Rice ＆ peanut milk material from becoming increasingly to glue and be difficult to stir.

Wherein, the lower puddling portion 252 is equipped with puddling blade 256 and lower puddling hole 250, and the lower puddling hole 250 is equal Even ground circle is opened on the puddling blade 256, and the puddling blade 256, which is tilted upward from the rotation axis 22 to both sides, to be prolonged It stretches, when the puddling blade 256 rotates, the lower puddling hole 250 helps to improve Rice ＆ peanut milk material in the turbulence of bottom, passes through institute That states puddling portion 251 and the lower puddling portion 252 coordinates so that the axial backmixing of Rice ＆ peanut milk material is stronger, and mass-transfer efficiency is high, to The conversion rate of starch granules is fast.

Wherein, the puddling blade 256 is equipped with intra vane 257 and outer leafs 258, and the intra vane 257 is integrally from institute State the protrusion of outer leafs 258 so that the puddling blade 256 formed it is step-like, in order to avoid stickum is adhered in plane and is difficult to It returns in Rice ＆ peanut milk material, while the rotating property of the puddling blade 256 also being avoided to decline.

Wherein, the angle between the puddling blade 256 in the lower puddling portion 252 is 110 °~130 °, it is preferable that described mixed The angle stirred between blade 256 is 120 °.

The gelatinization liquefied pot 20 is equipped with liquefaction feed mouth 201, liquefaction discharge port 202, lactic acid and adjusts mouth 203 and exhaust Mouth 204, the liquefaction feed mouth 201 and the exhaust outlet 204 are set to the top of the gelatinization liquefied pot 20, described to liquefy out Material mouth 202 is set to the bottom of the gelatinization liquefied pot 20, and the lactic acid adjusts mouth 203 and is set to the gelatinization liquefied pot 20 Top, the liquefaction feed mouth 201 are connected to the wet disintegrating apparatus 11, and the liquefaction discharge port 202 is connected to the blending tank 32, For adjusting the air pressure in the gelatinization liquefied pot 20, the lactic acid adjusts mouth 203 and is connected to the lactic acid exhaust outlet 204 Bacterium tank 31 is able to adjust the pH value in the gelatinization liquefied pot 20.

The gelatinization liquefied pot 20 further comprises that cleaning section 24, the cleaning section 24 are equipped with cleaning mouth 241 and rotation Cleaning ball 242, the spin-cleaning ball 242 are set in the gelatinization liquefied pot 20, are able to clean tank interior.

The steam jacket 23 is equipped with steam channel 231 and insulating layer 232, and it is logical that the insulating layer 232 coats the steam Road 231, the insulating layer 232 are polyethylene foamed.

The conveying equipment 14 includes bucket elevator 141, straining machine 142, pipe magnetic separator 15, measuring chute 16 and screw conveyor 17, the bucket elevator 141 is connected to the straining machine 142, and the pipe magnetic separator 15 is connected to the straining machine 142 and the measuring chute 16, the screw conveyor 17 is connected to the measuring chute 16 and the wet disintegrating apparatus 11, and the cleaner 12 is connected to described Straining machine 142, wherein the bucket elevator 141 for rice is delivered to the straining machine 142, the straining machine 142 with In removing the rubble impurity in rice, the cleaner 12 absorbs the dust in the straining machine 142, the pipe magnetic separator outward 15 for the irony clast in removal rice, and the measuring chute 16 is for the quantitative rice of conveying to the screw conveyor 17, then be delivered in the Roughpulverizer 18 by the screw conveyor 17.

Wherein, the cleaner 12 includes deduster 121, wind turbine 122, silencer 123 and dust removing tube 124, described Dust removing tube 124 is connected to the deduster 121 and the straining machine 142, and the wind turbine 122 is electrically connected to the cleaner 12, The silencer 123 connects the wind turbine 122, is able to eliminate the noise to it, reduces noise, improves working environment.

The wet disintegrating apparatus 11 further comprises shurry pump 188 and Pneumatic butterfly valve 189 of sizing mixing, the shurry pump 188 It is respectively arranged in the Roughpulverizer 18 and the slimer 19, the Pneumatic butterfly valve 189 of sizing mixing is separately connected described thick Pulverizer 18 and the slimer 19 are able to pneumatically adjust the thick disintegrating machine 18 and the slimer 19.

The Roughpulverizer 18 includes connections storehouse 181, guiding piece 184 and a pair of rolls last item 186, the guiding piece 184 It is rotationally arranged between the connections storehouse 181 and the roll-in axis 186, the connections storehouse 181 is connected to the screw rod transmission Machine 17, the periphery compartment of terrain of the guiding piece 184 are equipped with radially projecting, are able to guide the grain of rice to the roll-in axis by rotation Between 186, convenient for rolling, 186 relative rolling of roll-in axis pulverizes the grain of rice in water, and the Roughpulverizer 18 is equipped with water inlet Mouthful, it is able to the mixing grain of rice and hot water in the Roughpulverizer 18.

The Roughpulverizer 18 is equipped with hole 187 of sizing mixing, and the hole 187 of sizing mixing is set to the lower section of the roll-in axis 186, institute It states hole 187 of sizing mixing and is connected to the Pneumatic butterfly valve 189 of sizing mixing, be able to pneumatically being sized mixing in the Roughpulverizer 18 so that rice Grain is repeatedly rolled, and the grain size of the grain of rice is reduced.

The shurry pump 188 is set to the lower part of the Roughpulverizer 18, is able to Rice ＆ peanut milk material being pumped into the slimer In 19.

Wherein, the Roughpulverizer 18 is further provided with multiple Butterworth Hatch 185, is able to carry out the Roughpulverizer 18 CIP is cleaned.

Wherein, the Roughpulverizer 18 further comprises that level sensor 182 and liquid level sensor 183, the material position pass Sensor 182 is connected to the connections storehouse 181, is able to detect the controlling level of the connections storehouse 181, the liquid level sensor 183 connects The lower part for leading to the Roughpulverizer 18, is able to detect the liquid level of the Roughpulverizer 18.

The slimer 19 be equipped with cavity 191, first charging aperture 131, second charging aperture 132, the first discharge port 133, Second discharge port 132 and filter plate 192, the cavity 191 are equipped with chamber 193 fine crushing and filter chamber 194, the filter plate 192, which separate the cavity 191, forms the chamber fine crushing 193 and the filter chamber 194, the first charging aperture 131 and described the Two feed inlets 132 are located at the both sides at 19 top of the slimer, and first discharge port 133 is connected to the filter chamber 194 and extraneous, chamber 193 fine crushing and external world described in 133 lateral communication of the second discharge port, the connection of the first charging aperture 132 The Roughpulverizer 18 and the slimer 19 are able to by the first charging aperture 131 by the thick of the Roughpulverizer 18 Rice ＆ peanut milk is delivered to the slimer 19 and crushes, and the second charging aperture 132 is connected with second discharge port 134, When in the chamber 193 fine crushing grain of rice grain size or it is excessive when, pass through second discharge port 134 and the second charging aperture 132 back in the chamber fine crushing 193, are stirred crushing.

The slimer 19 includes decelerating motor 135, drive shaft 195, stirring parts 196 and axis fine crushing 198, described to subtract Speed motor 135 connects the drive shaft 195, and the drive shaft 195 is rotationally horizontally set at the upper of the chamber fine crushing 193 Portion, the stirring parts 196 are vertically connected to the both sides of the drive shaft 195 respectively, and the axis 198 fine crushing is set to the stirring The lower section of part 196, the stirring parts 196 are able to rotate with the drive shaft 195 while rotation, the axis 198 fine crushing Between gap 199 be less than the gap of the roll-in axis 186 in the Roughpulverizer 18, realize further refinement to Rice ＆ peanut milk.

Wherein, the stirring parts 196 are equipped with stirring blade 197, and the stirring blade 197 is uniform from the drive shaft 195 Compartment of terrain extends radially outwardly, and the stirring blade 197 is warp architecture, and the stirring blade 196 of each stirring parts 196 has 3.

Wherein, on the contrary, one tilts upward, one tilts downward the inclined direction of two stirring parts 196, is conducive to Stir more thorough, no dead angle.

Wherein, 195 eccentric rotation of the drive shaft, is able to stir more thorough, improves the slimer 19 Efficiency fine crushing.

Wherein, the axis fine crushing 198 is tooth type structures, and unpolished rice slurry is got enter into the gap between the axis fine crushing 198, It fine crushing rolls again but to its.

The shurry pump 188 is set in the filter chamber 192, is able to thin Rice ＆ peanut milk being pumped into the gelatinization liquefied pot 20 In.

A kind of preparation process of pure mellow wine preparation system 1, including step：

S100 prepares Rice ＆ peanut milk material, and rice and hot water are mixed, crushed in the wet disintegrating apparatus 11, forms Rice ＆ peanut milk Material；

S200 gelatinization liquefaction, is delivered to the gelatinization liquefied pot 20 by Rice ＆ peanut milk material, is heated and stirred by steam so that rice Interior starchiness expansion makes the grain of rice be gelatinized, and becomes starch granules, and liquefaction feed liquid is made, wherein the temperature of the gelatinization liquefied pot 20 Degree is 65~85 DEG C；

S300 feeds intake saccharification, and the distiller's yeast of the distiller's yeast tank 33 is delivered in the blending tank 32, then by the dextrin The liquefaction feed liquid changed in tank 20 is cooled to 10~20 DEG C after the tubular heat exchanger 34, into the blending tank 32, makes The feed liquid that must liquefy and distiller's yeast mix in stirring, and saccharification feed liquid is made, wherein distiller's yeast dosage is the 6%~8% of grain of rice raw material；

S400 ferments, and the saccharification feed liquid in the blending tank 32 is cooled down by the tubular heat exchanger 34, drops Temperature is to 10~16 DEG C, then enters in the fermentation tank 35, keeps 14~16 DEG C of the temperature of fermentation tank, and zymotic fluid is made；

S500 prepares pure mellow wine finished product, the pan-fried wine of system 40, storage wine, filtering and sterilizing after the fermentation by zymotic fluid Pure mellow wine finished product is made in process.

Wherein, the step S300 includes step：

S310, in the blending tank 32, keeps the blending tank 32 from distiller's yeast is put into the distiller's yeast tank 33 for the first time 17~19 DEG C of temperature；

S320 keeps the blending tank 32 from second of input distiller's yeast in the distiller's yeast tank 33 in the blending tank 32 28~32 DEG C of temperature；

S330, in the blending tank 32, keeps the blending tank 32 from distiller's yeast is put into the distiller's yeast tank 33 for the third time 22~25 DEG C of temperature.

To put into distiller's yeast in the blending tank 32 by multisection type, it is able to effectively allow aspergillus will liquefaction feed liquid sugar Change, if temperature is excessively high after feeding intake, saccharification is not thorough, if temperature is too low after feeding intake, harmful bacteria easy to pollute.

Wherein, the preparation process of the pure mellow wine preparation system 1 further comprises step：

S600 carries out pH value detection on the pipeline between the gelatinization liquefied pot 20 and the blending tank 32, if acidity is not Foot, then should mend acid, lactic acid bacteria is imported the gelatinization liquefied pot 20 and the blending tank 32 by the lactic acid bacteria tank 31, adjust The pH value of the gelatinization liquefied pot 20 and the blending tank 32, wherein pH value should control between 5.4~5.8, and preferably 5.6.

If pure mellow wine fermentation is not thorough, pleasantly sweet.

Wherein, the step S500 includes step：

S510 decocts wine, by separation of a part of zymotic fluid in the fermentation tank 35 through centrifuge 41 and settling tank 42, then It is delivered in the pan-fried wine system 43, another part zymotic fluid in the fermentation tank 35 is fed directly to the pan-fried wine system 43 Interior, then mix pan-fried wine, the temperature of the pan-fried wine system 43 is 80~90 DEG C, to not only allow colloid substances in zymotic fluid Matter condenses the harmful microorganism for keeping wine liquid as clear as crystal, and kill lactic acid bacteria and ferment etc. wine is made to addle, meanwhile, it mixes and decocts wine The freshness for being conducive to increase vinosity, improves biology and abiotic stability, improves vinosity；

Wine liquid is conveyed to stand into the wine storage tank 44 and be stored by S520 from the pan-fried wine system 43；

S530 cools down the wine liquid in the wine storage tank 44 by quickly cooling plate heat exchanger 45, then is delivered to described cold Jelly is blent to carry out freezing in tank 46 and be blent；

The freezing is blent the wine liquid in tank 46 and carries out multistage mistake by the filtration system 47 by S540 filtration sterilizations Filter forms finished product using sterilizing after the disinfection system 48, and sterilising temp is 62~64 DEG C.

A kind of filtration system 1C includes pre-filtrating equipment 10C and vertical blade filter 20C, the pre-filtrating equipment The upper ends 10C are equipped with feed pipe 11C, and lower end is equipped with discharge nozzle 12C, and the feed pipe 11C connections feeding equipment is able to upper single order Feed liquid in section is sent into the pre-filtrating equipment 10C, and the discharge nozzle 12C is connected to the vertical blade filter 20C, is able to The filtered filtrates of pre-filtrating equipment 10C are sent into the vertical blade filter 20C and carry out smart filtering, the pre- mistake Filter device 10C is installed on institute equipped with horizontal filtering blade 13C, agitating device 14C, circulator 15C, the agitating device 14C The upper ends horizontal filtering blade 13C are stated, is achieved and is stirred in filtering, accelerate filter efficiency, the circulator 15C is installed on It on the right side of the pre-filtrating equipment 10C, is achieved and is filtered for multiple times, the vertical blade filter 20C is equipped with vertical filter leaf The filter core aperture of 21C, the horizontal filtering blade 13C are more than the filter core aperture of the vertical filter leaf 21C, are achieved point Grade filtering, it is cost-effective to further increase filter efficiency.

Wherein, the filter core aperture of the pre-filtrating equipment 10C is 5 μm, when the pre-filtrating equipment 10C forms cake filtration When, the pre-filtrating equipment 10C is able to the impurity that filter diameter is not less than 1 μm, the filter core hole of the vertical blade filter 20C Diameter is 0.5 μm, and when the vertical blade filter 20C forms cake filtration, the vertical blade filter 20C is filtered Diameter is not less than 0.1 μm of impurity.

Wherein, the agitating device 14C is equipped with motor 141C and agitating paddle 142C, is stirred described in the motor 141C controls The operating for mixing paddle 142C starts the motor 141C when carrying out pre-filtering, and the motor 141C drives the agitating paddle 142C Feed liquid in the pre-filtrating equipment 10C is stirred, is achieved and is stirred in filtering, to accelerate filter efficiency.

Wherein, the circulator 15C includes check valve 151C and product pump 152C, and the check valve 151C is controlled Primary filtrate processed is uniaxially back to the pre-filtrating equipment 10C from lower end, and the product pump 152C sucks back primary filtrate described pre- Filter device 10C closes the liquid valve in the pre-filtrating equipment 10C, opens before the pre-filtrating equipment 10C is filtered The motor 141C is moved, the motor 141C drives the agitating paddle 142C rotations, the agitating paddle 142C to be able to described pre- Feed liquid in filter device 10C is stirred, and opens simultaneously the check valve 151C, and the check valve 151C is controlled initial filter Liquid is uniaxially back to the prefiltration device 10C from lower end, starts the product pump 152C, the product pump 152C be able to by It is for re-filtering that primary filtrate sucks back the upper end to the horizontal filtering blade 13C, is filtered for multiple times to realize；When the cycle After device 15C carries out circulating filtration 30min to primary filtrate, at this point, the filter cake covered on the horizontal filtering blade 13C forms filter Cake filters, and cake filtration is able to retain the impurity that diameter is not less than 1 μm, so as to further that grain size is miscellaneous not less than 1 μm Matter is retained down.

Wherein, the pre-filtrating equipment 10C is further provided with flowmeter 16C, backwashing system 17C, the flowmeter 16C It is able to detect the real time filtering flow of the pre-filtrating equipment 10C, the backwashing system 17C is installed on the pre-filtrating equipment The bottom ends 10C, the backwashing system 17C include Residue extraction pipeline 171C, and the Residue extraction pipeline 171C is installed on the pre-filtering dress The sides 10C are set, when refiltering a period of time, when observing that the flow of the flowmeter 16C is less than standard value, the pre- mistake described at this time Filter device 10C is basically completed, and is closed the circulator 15C, is opened simultaneously the liquid valve in the pre-filtrating equipment 10C, institute It states the filtrate in pre-filtrating equipment 10C to get enter into the vertical blade filter 20C, proceeds by smart filtering.

Wherein, after the pre-filtrating equipment 10C completes to filter, the backwashing system 17C, the backwash system are opened System 17C be able to be rinsed the pre-filtrating equipment 10C, then by the waste residue after flushing by the Residue extraction pipeline 171C into Row discharge.

Wherein, the vertical blade filter 20C is equipped with charging cavity 22C and discharging cavity 23C, the vertical filtering Blade 21C is set in the vertical blade filter 20C, is able to the vertical blade filter 20C being divided into two parts, It forms the charging cavity 22C and the discharging cavity 23C, the charging cavity 22C and the discharging cavity 23C sets up separately In the both sides vertical filter leaf 21C, it is able to primary filtrate from the charging cavity 22C laterally through the vertical filtering Blade 21C is filtered to the discharging cavity 23C, to complete vertical filtering.

Wherein, the vertical blade filter 20C further comprises negative pressure device 24C, cleaning device 25C and dress of slagging tap 26C is set, the negative pressure device 24C is connected to the discharging cavity 23C, is able to evacuate the discharging cavity 23C, described Cleaning device 25C is installed on the upper ends vertical blade filter 20C, is able to filter the vertical blade after the completion of filtering Machine 20C is cleaned, and the deslagging device 26C is installed on the lower ends vertical blade filter 20C, is able to useless after cleaning Slag is discharged by the deslagging device 26C.

Wherein, the negative pressure device 24C further comprises vacuum pump 241C, negative-pressure pipeline 242C, negative pressure valve 243C, institute It states negative-pressure pipeline 242C and is connected to the discharging cavity 23C, the negative pressure valve 243C is installed on the negative-pressure pipeline 242C, institute Vacuum pump 241C is stated to be able to evacuate the discharging cavity 23C by the negative-pressure pipeline 242C, when carrying out essence filtering, The primary filtrate enters the charging cavity 22C from the discharge nozzle 12C of the pre-filtrating equipment 10C, starts the vacuum 241C is pumped, opens the negative pressure valve 243C, the vacuum pump 241C is able to through the negative-pressure pipeline 242C to the discharging Cavity 23C is evacuated, at this point, the pressure value of the discharging cavity 23C and the charging cavity 22C are able to difference, is formed Pressure difference, to push primary filtrate to be filtered from the charging cavity 22C to described laterally through the vertical filter leaf 21C Discharge cavity 23C, simultaneously because the effect of pressure difference, the liquid in filter cake can also be squeezed out, be improved filter efficiency.

Wherein, the vertical filter leaf 21C is multiple filtration blade, is achieved and successively filters, makes filtered filter Liquid is more clarified, and the apertures of the vertical filter leaf 21C from left to right become smaller successively, so as to layer by layer by different-diameter Impurity is filtered step by step, to ensure that filtering fast and effeciently carries out.

Wherein, multiple protrusion 211C, multiple protrusion 211C dispersions are further provided on the vertical filter leaf 21C In on the vertical filter leaf 21C, being reduced adhesion strength of the filter cake on the vertical filter leaf 21C, to clear It is brought convenience during filter wash cake.

Wherein, the cleaning device 25C further comprises cleaning sprayer 251C, compression pump 252C, the first valve 253C, defeated Pipeline 254C, the cleaning sprayer 251C is sent to be directed at the vertical filter leaf 21C, the compression pump 252C is able to cleaning agent It is sent to the cleaning sprayer 251C, the first valve 253C by the conveyance conduit 254C and controls the cleaning sprayer 251C Open or close open the compression pump 252C and the first valve 253C, the compression pump 252C after the completion of filtering Be able to by the conveyance conduit 254C send detergent to the cleaning sprayer 251C, the quantity of the cleaning sprayer 251C with The number of plies of the vertical filter leaf 21C is corresponding, is able to be rinsed vertical filter leaf 21C described in every layer, Mei Gesuo It states above the gap that cleaning sprayer 251C is installed between two vertical filter leaf 21C, every layer of vertical filter leaf excessively Opposite on piece 21C there are one the cleaning sprayer 251C, are able to the filter cake and impurity on every layer of vertical filter leaf 21C Washing removing is carried out, the cleaning sprayer 251C is able to be rinsed the filter cake being adhered on the vertical filter leaf 21C, Filter cake wash and be rinsed the vertical filter leaf 21C from being done directly, and passes through the dress of slagging tap Set 26C by after washing filter cake and detergent be discharged, to complete filtering, cleaning, deslagging process, realize a tractor serves several purposes, behaviour Make simple and convenient.

Basic principles, main features, and advantages of the present invention has been shown and described above.One's own profession The technical staff of industry is it should be appreciated that the present utility model is not limited to the above embodiments, described in above embodiments and description Only the principles of the present invention, on the premise of not departing from the spirit and scope of the utility model the utility model also have respectively Kind changes and improvements, these changes and improvements are both fallen in claimed the scope of the utility model.The requires of the utility model Protection domain defined by appended claims and its equivalent.

Claims (10)

1. a kind of wet disintegrating apparatus, which is characterized in that including Roughpulverizer and slimer, the Roughpulverizer connection conveying Equipment and the slimer, the dry grain of rice and hot water are mixed into the Roughpulverizer, are able to carry out preliminary crushing to the grain of rice, In, the Roughpulverizer includes connections storehouse, guiding piece and a pair of rolls last item, and the guiding piece is rotationally arranged at the company It connects between storehouse and the roll-in axis, the connections storehouse is connected to conveying equipment, and the periphery compartment of terrain of the guiding piece is equipped with radial dash forward Go out, be able to guide the grain of rice between the roll-in axis by rotation, the Roughpulverizer is equipped with water inlet, is able to described thick The mixing grain of rice and hot water in pulverizer.

2. wet disintegrating apparatus according to claim 1, which is characterized in that the wet disintegrating apparatus further comprises shurry pump And Pneumatic butterfly valve of sizing mixing, the shurry pump are respectively arranged in the Roughpulverizer and the slimer, the gas of sizing mixing Dynamic butterfly valve is separately connected the Roughpulverizer and the slimer, is able to carry out the thick disintegrating machine and the slimer It is pneumatic to adjust.

3. wet disintegrating apparatus according to claim 2, which is characterized in that the Roughpulverizer is equipped with hole of sizing mixing, the tune Slurry hole is set to the lower section of the roll-in axis, the Pneumatic butterfly valve of sizing mixing described in the connection of hole of sizing mixing.

4. wet disintegrating apparatus according to claim 3, which is characterized in that the Roughpulverizer further comprises that material position senses Device and liquid level sensor, the level sensor is connected to the connections storehouse, is able to detect the controlling level of the connections storehouse, described Liquid level sensor is connected to the lower part of the Roughpulverizer, is able to detect the liquid level of the Roughpulverizer.

5. wet disintegrating apparatus according to claim 4, which is characterized in that the slimer is equipped with cavity, the first charging Mouth, second charging aperture, the first discharge port, the second discharge port and filter plate, the cavity are equipped with chamber fine crushing and filter chamber, institute State filter plate and separate the cavity and form the chamber fine crushing and the filter chamber, the first charging aperture and with second charging Mouth is located at both sides at the top of the slimer, and first discharge port is connected to the filter chamber and the external world, and described second Chamber and the external world, the first charging aperture connection Roughpulverizer and the slimer fine crushing described in discharge port lateral communication, It is able to the unpolished rice of Roughpulverizer slurry being delivered to the slimer by the first charging aperture and crush, described the Two feed inlets are connected with second discharge port.

6. wet disintegrating apparatus according to claim 5, which is characterized in that the slimer includes decelerating motor, driving Axis, stirring parts and axis fine crushing, the decelerating motor connect the drive shaft, and the drive shaft is rotationally horizontally set at institute The top of chamber fine crushing is stated, the stirring parts are vertically connected to the both sides of the drive shaft respectively, and the axis fine crushing is set to described The lower section of stirring parts, the gap between the axis fine crushing are less than the gap of the roll-in axis in the Roughpulverizer.

7. wet disintegrating apparatus according to claim 6, which is characterized in that the stirring parts are equipped with stirring blade, described to stir Blade is mixed to be evenly spaced apart to extend radially outwardly from the drive shaft.

8. wet disintegrating apparatus according to claim 7, which is characterized in that the stirring blade is warp architecture, Ge Gesuo The stirring blade for stating stirring parts has 3.

9. wet disintegrating apparatus according to claim 8, which is characterized in that the inclined directions of two stirring parts on the contrary, One tilts upward, and one tilts downward.

10. wet disintegrating apparatus according to claim 9, which is characterized in that the axis fine crushing is tooth type structures, and unpolished rice is starched To enter in the gap between the axis fine crushing.