CN216571588U

CN216571588U - Tower type rectifying distiller

Info

Publication number: CN216571588U
Application number: CN202123319431.9U
Authority: CN
Inventors: 郭辉
Original assignee: Hubei Paris Flavor Food Co ltd
Current assignee: Hubei Paris Flavor Food Co ltd
Priority date: 2021-12-27
Filing date: 2021-12-27
Publication date: 2022-05-24
Anticipated expiration: 2031-12-27

Abstract

The utility model relates to the technical field of wine processing equipment, and discloses a tower type rectifying distiller, which comprises a distillation tank, a rectifying tower and a condenser, the top end of the distillation tank is communicated with the bottom of the rectifying tower through a first draft tube which is communicated with the inside of the distillation tank, the top of the rectifying tower is communicated with the condenser through a flow guide pipe II, the bottom of the condenser is communicated with a liquid outlet pipe, the bottom of the distillation tank is communicated with a sewage discharge pipe, the inside of the distillation tank is provided with a stirring mechanism, the stirring mechanism comprises a stirring shaft and a driving motor, the driving motor is arranged at the top end of the distillation retort, the stirring shaft is vertically arranged in the distillation retort, the top end of the stirring shaft extends out of the top of the distillation retort and is connected with an output shaft of the driving motor, and a plurality of stirring rods and stirring blades are arranged on the outer wall of the stirring shaft. The utility model discloses a tower rectification distiller can effectively improve the heating efficiency of retort, improves distillation efficiency and alcohol purity.

Description

Tower type rectifying distiller

Technical Field

The utility model relates to a drinks processing equipment technical field, in particular to tower rectification distiller.

Background

The wine brewing process mainly comprises the steps of raw material crushing, saccharification, fermentation, distillation, storage and the like, wine liquid distillation equipment is key equipment for distilling and purifying alcohol, in order to brew wine with better taste in the prior art, multiple times of distillation can be generally carried out in the distillation process so as to obtain the wine with higher purity, but the existing distillation equipment has low heating efficiency and insufficient heat utilization, so that the distillation time is long, and the processing efficiency and the quality are influenced.

SUMMERY OF THE UTILITY MODEL

The utility model discloses an aim at overcoming prior art's defect, provide a tower rectification distiller, can effectively improve the heating efficiency of retort, improve distillation efficiency and alcohol purity.

The above technical object of the present invention can be achieved by the following technical solutions: a tower type rectifying distiller comprises a distillation retort, a rectifying tower and a condenser, wherein the top end of the distillation retort is communicated with the bottom of the rectifying tower through a first flow guide pipe, the first flow guide pipe is communicated with the inside of the distillation retort, the top of the rectifying tower is communicated with the condenser through a second flow guide pipe, the bottom of the condenser is communicated with a liquid outlet pipe, a liquid outlet valve is arranged on the liquid outlet pipe, the bottom of the distillation retort is communicated with a sewage discharge pipe, a sewage discharge valve is arranged on the sewage discharge pipe, a stirring mechanism is arranged inside the distillation retort and comprises a stirring shaft and a driving motor, the driving motor is arranged at the top end of the distillation retort, the stirring shaft is vertically arranged in the distillation retort, the top end of the stirring shaft extends out of the top of the distillation retort and is connected with an output shaft of the driving motor, and a plurality of stirring rods and stirring blades are arranged on the outer wall of the stirring shaft, the stirring rod and the stirring blades are arranged in a staggered mode at intervals along the axial direction of the stirring shaft.

The utility model discloses a further set up to: the stirring rod comprises a transverse rod and a vertical rod, a plurality of transverse rods are arranged on the outer wall of the stirring shaft at even intervals along the axial direction, the middle of the transverse rod is fixedly connected with the stirring shaft, the vertical rods are arranged at the two ends of the transverse rod, and the vertical rods are arranged in parallel with the stirring shaft.

The utility model discloses a further set up to: the stirring paddle comprises long blades and short blades, the long blades and the short blades are arranged in a staggered mode along the circumferential direction of the stirring shaft at intervals, and a plurality of through holes are formed in the long blades and the short blades.

The utility model discloses a further set up to: the retort is including outer casing and the inlayer jar of body, outer casing with be provided with the heating chamber between the inlayer jar of body, the heating intracavity is provided with the heating pipe, the heating pipe is the heliciform and encircles on the outer wall of the inlayer jar of body.

The utility model discloses a further set up to: the bottom of the rectifying tower is communicated with a return pipe, one end of the return pipe, which is far away from the rectifying tower, is communicated with the bottom of the distillation tank, and the return pipe is provided with a return valve.

The utility model discloses a further set up to: and an observation window is arranged on the outer wall of the rectifying tower.

The utility model discloses a further set up to: the condenser is a horizontal condenser, the bottom ends of the two diversion pipes are communicated with one end of the condenser, the liquid outlet pipe is arranged at the position, away from the other end of the second diversion pipe, of the condenser, a spiral condensation pipe is arranged in the condenser, the condenser is close to the bottom of one end of the liquid outlet pipe, and a water outlet pipe is arranged at the top of one end of the two diversion pipes, close to the condenser.

The utility model discloses a further set up to: a filter screen is arranged at the water inlet pipe.

The utility model has the advantages that: the utility model discloses a tower rectification distiller, through set up rabbling mechanism in the retort, when heating wine liquid raw materials, start driving motor, the drive (mixing) shaft rotates, drive puddler and stirring paddle leaf stir wine liquid raw materials, it is more even to make wine liquid raw materials be heated, heating efficiency is improved, puddler and the crisscross setting in stirring paddle leaf interval, make the wine liquid raw materials of the different degree of depth receive different stirring power sizes in the retort, thereby obtain different velocities of motion, make wine liquid raw materials in the retort be in the motion state all the time, ensure the heating effect, thereby improve distillation efficiency.

Drawings

In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings used in the description of the embodiments will be briefly described below, and it is obvious that the drawings in the description are only some embodiments of the present invention, and it is obvious for those skilled in the art that other drawings can be obtained without creative efforts.

FIG. 1 is a schematic diagram of the overall structure of a tower type distillation apparatus according to the present invention;

FIG. 2 is a schematic cross-sectional view of a distillation tank of a tower-type distillation still according to the present invention;

FIG. 3 is a schematic structural view of a distillation tank stirring blade of the tower type rectification distiller of the present invention;

fig. 4 is a schematic sectional view of a condenser of a tower-type distillation apparatus according to the present invention.

In the figure, 1, a distillation retort, 11, a blow-off pipe, 12, a blow-off valve, 13, an outer shell, 14, an inner tank body, 15, a heating cavity, 16 and a heating pipe; 2. a rectifying tower 21 and an observation window; 3. the condenser 31, the liquid outlet pipe 32, the liquid outlet valve 33, the condenser pipe 34, the water inlet pipe 35 and the water outlet pipe; 4. a flow guide pipe I; 5. a second flow guide pipe; 6. the stirring mechanism comprises a stirring mechanism 61, a stirring shaft, 62, a driving motor 63, a stirring rod 631, a cross rod 632, a vertical rod 64, a stirring blade 641, a long blade 642, a short blade 643 and a through hole; 7. a return pipe 71, a return valve.

Detailed Description

The technical solution of the present invention will be clearly and completely described below with reference to the specific embodiments. It is obvious that the described embodiments are only some of the embodiments of the present invention, and not all of them. Based on the embodiments of the present invention, all other embodiments obtained by a person of ordinary skill in the art without creative efforts belong to the protection scope of the present invention.

Referring to fig. 1 and 2, a tower type rectifying still comprises a distillation retort 1, a rectifying tower 2 and a condenser 3, wherein the top end of the distillation retort 1 is communicated with the bottom of the rectifying tower 2 through a first diversion pipe 4, the first diversion pipe 4 is communicated with the inside of the distillation retort 1, the top of the rectifying tower 2 is communicated with the condenser 3 through a second diversion pipe 5, the bottom of the condenser 3 is communicated with a liquid outlet pipe 31, a liquid outlet valve 32 is arranged on the liquid outlet pipe 31, the bottom of the distillation retort 1 is communicated with a sewage discharge pipe 11, a sewage discharge valve 12 is arranged on the sewage discharge pipe 11, a stirring mechanism 6 is arranged inside the distillation retort 1, the stirring mechanism 6 comprises a stirring shaft 61 and a driving motor 62, the driving motor 62 is arranged at the top end of the distillation retort 1, the stirring shaft 61 is vertically arranged in the distillation retort 1, the top end of the stirring shaft 61 extends out of the top of the distillation retort 1 and is connected with an output shaft of the driving motor 62, a plurality of stirring rods 63 and stirring blades 64 are arranged on the outer wall of the stirring shaft 61, the stirring rods 63 and the stirring blades 64 are alternately arranged along the axial direction of the stirring shaft 61. Use the utility model discloses a during tower rectification distiller, pour the wine liquid raw materials into retort 1 in and heat, after the temperature risees, the wine liquid to retort 1 in begins to distill, wine steam carries out the rectification in getting into rectifying column 2 through honeycomb duct one 4, further improve the purity of alcohol, wine steam arrives in condenser 3 through honeycomb duct two 5 after the rectification in, condenser 3 condenses wine steam, make wine steam become the liquid back through the 31 ejection of compact of drain pipe, after the processing is accomplished, can wash in retort 1, discharge sewage through blow off pipe 11. Through setting up rabbling mechanism 6 in retort 1, when heating the wine liquid raw materials, through starting driving motor 62, drive (mixing) shaft 61 rotates, drive puddler 63 and stirring paddle leaf 64 stir the wine liquid raw materials, it is more even to make the wine liquid raw materials be heated, improve heating efficiency, puddler 63 and the crisscross setting in stirring paddle leaf 64 interval, make the wine liquid raw materials of the different degree of depth receive different stirring power sizes in retort 1, thereby obtain different velocities of motion, make the wine liquid raw materials in retort 1 be in the motion state all the time, ensure the heating effect, thereby improve distillation efficiency.

Referring to fig. 2 and 3, puddler 63 includes horizontal pole 631 and montant 632, be provided with a plurality of horizontal pole 631 along the even interval of axial on the (mixing) shaft 61 outer wall, the middle part and the (mixing) shaft 61 fixed connection of horizontal pole 631, the both ends of horizontal pole 631 all are provided with montant 632, montant 632 and (mixing) shaft 61 parallel arrangement, horizontal pole 631 and montant 632's setting, make puddler 63 structure more firm, stir the wine liquid raw materials in retort 1 from horizontal direction and vertical direction simultaneously, make the wine liquid move towards different directions, ensure to be heated more evenly. The stirring paddle 64 comprises long blades 641 and short blades 642, the long blades 641 and the short blades 642 are arranged at intervals in a staggered mode along the circumferential direction of the stirring shaft 61, so that a speed vector which is close to the stirring paddle 64 is generated by the stirred wine liquid in the stirring process, the abrasion to the stirring paddle 64 is reduced, a plurality of through holes 643 are formed in the long blades 641 and the short blades 642, the wine liquid can pass through the through holes 643, and the resistance of the stirring paddle 64 in the stirring process is reduced.

Referring to fig. 2, retort 1 is including outer casing 13 and the inlayer jar body 14, is provided with heating chamber 15 between outer casing 13 and the inlayer jar body 14, is provided with heating pipe 16 in the heating chamber 15, and heating pipe 16 is the heliciform and encircles on the outer wall of the inlayer jar body 14 for the inside wine liquid of the inlayer jar body 14 is whole to be heated evenly, further improves retort 1's heating efficiency, and heat utilization rate is high, thereby improves distillation effect and alcohol purity.

Referring to fig. 1, the bottom of rectifying column 2 communicates with return pipe 7, the one end that the rectifying column 2 was kept away from to return pipe 7 communicates with retort 1 bottom, be provided with backward flow valve 71 on the return pipe 7, when distilling the wine liquid raw materials through retort 1, when the temperature reaches a certain degree, various materials in the raw materials begin to evaporate in succession and become gaseous rising, get into in rectifying column 2 through honeycomb duct one 4, further purify steam, the higher steam of purity continues to rise, reach condenser 3 through honeycomb duct two 5 and carry out the condensation ejection of compact, and have the not high steam condensation of partial purity to become liquid in the rectifying column 2, flow into retort 1 through return pipe 7 and carry out the secondary distillation. Be provided with observation window 21 on the rectifying column 2 outer wall, be convenient for observe the condition in rectifying column 2.

Referring to fig. 4, the condenser 3 is a horizontal condenser 3, the bottom of the second 5 of honeycomb ducts communicates with the one end of the condenser 3, drain pipe 31 sets up the other end of the second 5 of honeycomb ducts of keeping away from at the condenser 3, be provided with spiral helicine condenser pipe 33 in the condenser 3, the bottom that the condenser 3 is close to drain pipe 31 one end is provided with inlet tube 34, the top that the condenser 3 is close to the second 5 one end of honeycomb ducts is provided with outlet pipe 35, make cooling water get into in the condenser 3 through inlet tube 34, condense it when steam passes through condenser pipe 33, inlet tube 34 sets up the one end of keeping away from steam entering, can fully ensure the condensation effect to steam, make steam can become liquid completely and flow out from drain pipe 31, condenser pipe 33 sets up to the heliciform, the condensation time of steam has been improved, ensure the condensation effect. The filter screen is arranged at the position of the water inlet pipe 34, so that impurities in the cooling water can be filtered, excessive impurities are prevented from entering the condenser 3, and the inside of the condenser is prevented from generating accumulated scale, so that the condensing effect is influenced.

Claims

1. A tower type rectifying distiller is characterized in that: comprises a distillation retort (1), a rectifying tower (2) and a condenser (3), wherein the top end of the distillation retort (1) is communicated with the bottom of the rectifying tower (2) through a first diversion pipe (4), the first diversion pipe (4) is communicated with the inside of the distillation retort (1), the top of the rectifying tower (2) is communicated with the condenser (3) through a second diversion pipe (5), the bottom of the condenser (3) is communicated with a liquid outlet pipe (31), the liquid outlet pipe (31) is provided with a liquid outlet valve (32), the bottom of the distillation retort (1) is communicated with a sewage discharge pipe (11), the sewage discharge pipe (11) is provided with a sewage discharge valve (12), the distillation retort (1) is internally provided with a stirring mechanism (6), the stirring mechanism (6) comprises a stirring shaft (61) and a driving motor (62), the driving motor (62) is arranged at the top end of the distillation retort (1), the stirring shaft (61) is vertically arranged in the distillation tank (1), the top end of the stirring shaft (61) extends out of the top of the distillation tank (1) and is connected with an output shaft of the driving motor (62), a plurality of stirring rods (63) and stirring blades (64) are arranged on the outer wall of the stirring shaft (61), and the stirring rods (63) and the stirring blades (64) are arranged in a staggered mode at axial intervals of the stirring shaft (61).

2. The tower rectifier still of claim 1, wherein: puddler (63) include horizontal pole (631) and montant (632), be provided with a plurality of horizontal pole (631) along the even interval of axial on (mixing) shaft (61) outer wall, the middle part of horizontal pole (631) with (mixing) shaft (61) fixed connection, the both ends of horizontal pole (631) all are provided with montant (632), montant (632) with (mixing) shaft (61) parallel arrangement.

3. The tower rectifier still of claim 1, wherein: the stirring paddle (64) comprises long blades (641) and short blades (642), the long blades (641) and the short blades (642) are arranged in a staggered mode at intervals along the circumferential direction of the stirring shaft (61), and a plurality of through holes (643) are formed in each of the long blades (641) and the short blades (642).

4. The tower rectifier still of claim 1, wherein: retort (1) is including outer casing (13) and the inlayer jar body (14), outer casing (13) with be provided with heating chamber (15) between the inlayer jar body (14), be provided with heating pipe (16) in heating chamber (15), heating pipe (16) are the heliciform and encircle on the outer wall of the inlayer jar body (14).

5. The tower rectifier still of claim 1, wherein: the bottom of rectifying column (2) communicates there is back flow (7), back flow (7) are kept away from the one end of rectifying column (2) with retort (1) bottom intercommunication, be provided with reflux valve (71) on back flow (7).

6. The tower rectifier still of claim 1, wherein: an observation window (21) is arranged on the outer wall of the rectifying tower (2).

7. The tower rectifier still according to any one of claims 1 to 6, wherein: condenser (3) is horizontal condenser (3), honeycomb duct two (5) bottom with the one end intercommunication of condenser (3), drain pipe (31) set up condenser (3) are kept away from the other end of honeycomb duct two (5), be provided with spiral helicine condenser pipe (33) in condenser (3), condenser (3) are close to the bottom of drain pipe (31) one end is provided with inlet tube (34), condenser (3) are close to the top of honeycomb duct two (5) one end is provided with outlet pipe (35).

8. The tower rectifier still of claim 7, wherein: a filter screen is arranged at the position of the water inlet pipe (34).