CN213202997U

CN213202997U - White spirit production distillation plant

Info

Publication number: CN213202997U
Application number: CN202021829876.4U
Authority: CN
Inventors: 刘文涛
Original assignee: Henan Wanggong Liquor Co ltd
Current assignee: Henan Wanggong Liquor Co ltd
Priority date: 2020-08-28
Filing date: 2020-08-28
Publication date: 2021-05-14
Anticipated expiration: 2030-08-28

Abstract

The utility model discloses a white spirit production distillation equipment, including the end pot, the end pot upside sets up the rice steamer bucket, rice steamer bucket upside sets up the rice steamer lid, the rice steamer lid connects the vapour-liquid pipe, vapour-liquid pipe sets up centrifugal fan with rice steamer lid junction, vapour-liquid pipe end sets up the condensing box, condensing box upper portion sets up the heat exchange tubulation, the upper and lower ends of heat exchange tubulation are connected cloth case and collection box respectively, the heat exchange spiral pipe is connected to the collection box downside, the end of heat exchange spiral pipe connects the separator box, the separator box connects wine outlet pipe and first muffler, vapour-liquid pipe outside cover establishes the pre-condensation pipe, first muffler is connected with the pre-condensation, the pre-condensation pipe connects the second muffler, the second muffler connects the three-way valve, the three-way valve connects third muffler and blast pipe respectively, the third muffler connects the rice steamer bucket; the utility model is provided with the centrifugal fan, and actively guides the steam to promote condensation, thereby improving the distillation efficiency; the gas-liquid separation of the wine outlet end is realized, the pre-condensation is realized by utilizing the residual cold of the separated gas, and the condensation effect is good.

Description

White spirit production distillation plant

Technical Field

The utility model belongs to the technical field of white spirit production distillation plant, concretely relates to white spirit production distillation plant.

Background

White spirit is a common beverage which is deeply popular with people. The Chinese population is large, the wine demand is large, the wine making history is long, the technology is mature, the wine making resources are rich, the local materials can be used, and the superior conditions are created for brewing the white spirit. Therefore, it is made in remote rural areas as well as in some small production enterprises or wine studios. The application of liquor retort distillation is an important step in the production of white liquor. In the step, ethanol and other fragrant substances in the vinasse are vaporized into wine vapor through distillation of the wine retort, and then the wine vapor is introduced into a condensing device to be condensed and cooled to produce the finished product white spirit. The traditional distillation device consists of a bottom pot, a wine retort and a condensing device, wherein the wine retort is connected with an inlet of a condensing reflux device in the condensing device through a wine steam conveying pipe, the condensing device is provided with a cooling water inlet pipe and a cooling water outlet pipe, and the lower end of the condenser is provided with a wine outlet pipe. With the development of wine making technology, although bottom pots, wine retorts and condensing units are greatly improved, the existing distilling device is guided to the condensing unit by steam pressure, so that the efficiency is low, the condensation is insufficient, and the effect is poor.

SUMMERY OF THE UTILITY MODEL

The utility model aims at providing a white spirit production distillation equipment, which solves the problems in the prior art, is provided with a centrifugal fan, actively guides steam to promote condensation and improves distillation efficiency; the gas-liquid separation of the wine outlet end is realized, the pre-condensation is realized by utilizing the residual cold of the separated gas, and the condensation effect is good.

In order to achieve the above object, the utility model provides a following technical scheme: a white spirit production distillation device comprises a bottom pot, wherein a steaming barrel is arranged on the upper side of the bottom pot, an interlayer is arranged on the inner side of the side wall of the steaming barrel, a cavity is formed between the interlayer and the side wall of the steaming barrel, the lower end of the cavity is communicated with the inside of the steaming barrel, a steaming cover is arranged on the upper side of the steaming barrel, a vapor-liquid conduit is connected with the steaming cover, a centrifugal fan is arranged at the joint of the vapor-liquid conduit and the steaming cover and guides fluid in the steaming barrel and the steaming cover into the vapor-liquid conduit, a condensing box is arranged at the tail end of the vapor-liquid conduit, a plurality of vertical heat exchange tubes are arranged at the upper part of the condensing box, a material distribution box and a liquid collection box are respectively connected at the upper end and the lower end of the heat exchange tubes, the material distribution box is connected with the vapor-liquid conduit, a heat exchange spiral tube is connected with the lower, the tail end of the first air return pipe is connected with one end of the pre-condensation pipe, the other end of the pre-condensation pipe is connected with a second air return pipe, the second air return pipe is connected with a three-way valve, the three-way valve is further respectively connected with a third air return pipe and an exhaust pipe, and the third air return pipe is connected to the upper portion of the retort barrel and communicated with the cavity.

Further, a gap is formed between the lower end of the interlayer and the bottom of the retort barrel.

Further, a cooling medium inlet pipe and a cooling medium outlet pipe are respectively provided at the lower portion and the upper portion of the condensation tank.

Furthermore, valves are arranged on the cooling medium inlet pipe, the cooling medium outlet pipe and the wine outlet pipe.

Furthermore, the middle part of the separation box is connected with the heat exchange spiral pipe, and the upper part of the separation box is provided with a plurality of layers of filter screens.

The utility model has the advantages as follows:

the utility model is provided with the centrifugal fan, and the steam generated in the steamer barrel is actively guided to enter the condensation to promote the condensation through the driving action of the centrifugal fan, so that the distillation efficiency is greatly improved; the gas-wine separation at the wine outlet end is realized for non-condensed gas, and the pre-condensation of vapor and liquid led out of the retort barrel is realized by utilizing the residual cold of the cooling separation gas, so that the energy is saved, and the condensation effect is good.

Drawings

Fig. 1 is a schematic structural diagram of the present invention.

In the figure: 1. the device comprises a bottom pot, 2, a retort barrel, 3, a retort cover, 4, a vapor-liquid guide pipe, 5, a centrifugal fan, 6, a condensation box, 7, a separation box, 8, a pre-condensation pipe, 9, a second air return pipe, 10, a three-way valve, 11, a third air return pipe, 12, an exhaust pipe, 21, an interlayer, 61, a heat exchange tube array, 62, a material distribution box, 63, a liquid collection box, 64, a heat exchange spiral pipe, 65, a cooling medium inlet pipe, 66, a cooling medium discharge pipe, 71, a wine outlet pipe, 72, a first air return pipe, 73 and a filter screen.

Detailed Description

The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.

In the description of the present invention, it is to be understood that the terms "middle", "length", "width", "thickness", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", and the like indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are only for convenience of description and simplicity of description, and do not indicate or imply that the device or element referred to must have a particular orientation, be constructed and operated in a particular orientation, and therefore, should not be construed as limiting the present invention.

Furthermore, the terms "first", "second" and "first" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implicitly indicating the number of technical features indicated. Thus, a feature defined as "first" or "second" may explicitly or implicitly include one or more of that feature.

In the present invention, unless otherwise expressly stated or limited, the terms "mounted," "connected," and "fixed" are to be construed broadly and may, for example, be fixedly connected, detachably connected, or integrally formed; either directly or indirectly through intervening media, either internally or in any other relationship. The specific meaning of the above terms in the present invention can be understood according to specific situations by those skilled in the art.

Referring to fig. 1, the embodiment provides a white spirit production distillation apparatus, which comprises a bottom pan 1, wherein a retort barrel 2 is arranged on the upper side of the bottom pan 1, an interlayer 21 is arranged on the inner side of the side wall of the retort barrel 2, a cavity is formed between the interlayer 21 and the side wall of the retort barrel 2, the lower end of the cavity is communicated with the interior of the retort barrel 2, a retort cover 3 is arranged on the upper side of the retort barrel 2, the retort cover 3 is connected with a vapor-liquid conduit 4, a centrifugal fan 5 is arranged at the joint of the vapor-liquid conduit 4 and the retort cover 3, the centrifugal fan 5 guides fluid in the retort barrel 2 and the retort cover 3 into the vapor-liquid conduit 4, a condensation box 6 is arranged at the tail end of the vapor-liquid conduit 4, a plurality of vertical heat exchange tubes 61 are arranged at the upper part of the condensation box 6, the upper end and the lower end of the heat exchange tubes 61 are respectively connected with a material distribution box 62 and a liquid collection box 63, the lower end and the upper end of the separation box 7 are respectively connected with a wine outlet pipe 71 and a first air return pipe 72, the outer side of the vapor-liquid guide pipe 4 is sleeved with a pre-condensation pipe 8, the tail end of the first air return pipe 72 is connected with one end of the pre-condensation pipe 8, the other end of the pre-condensation pipe 8 is connected with a second air return pipe 9, the second air return pipe 9 is connected with a three-way valve 10, the three-way valve 10 is further respectively connected with a third air return pipe 11 and an exhaust pipe 12, and the third air return pipe 11 is connected to the upper.

In this embodiment, a gap is formed between the lower end of the interlayer 21 and the bottom of the retort 2.

In the present embodiment, the lower portion and the upper portion of the condensation tank 6 are provided with a cooling medium inlet pipe 65 and a cooling medium outlet pipe 66, respectively.

In this embodiment, the cooling medium inlet pipe 65, the cooling medium outlet pipe 66 and the wine outlet pipe 71 are all provided with valves.

In this embodiment, the middle of the separation box 7 is connected with the heat exchange spiral pipe 64, and the upper part of the separation box 7 is provided with a plurality of layers of filter screens 73.

When the utility model is implemented, the bottom pot 1 is heated, so that the vinasse placed in the bottom pot 1 generates steam which passes through the bottom of the retort barrel 2 and enters the retort barrel 2; the centrifugal fan 5 works to efficiently bring the steam generated in the retort barrel 2 into the steam-liquid guide pipe 4 and convey the steam into the material distribution box 62 of the condensing box 6; a circulating cooling medium is provided in the condensation tank 6, and circulation and heat exchange of the cooling medium are realized through a cooling medium inlet pipe 65 and a cooling medium outlet pipe 66; the steam fluid passes through the material distribution box 62, the heat exchange tube array 61 and the liquid collection box 63 of the condensation box 6, and is condensed by exchanging heat with a cooling medium; the liquid and the uncondensed vapor pass through the heat exchange spiral pipe 64 to be further subjected to heat exchange to realize full condensation; the condensed white spirit is guided into the separating box 7 from the heat exchange spiral pipe 64, and the gas which is not condensed passes through the filter screen 73 and enters the first air return pipe 72; the white spirit is discharged through the valve of the spirit outlet pipe 71; the uncondensed gas is subjected to sufficient heat exchange temperature reduction in the condensation box 6, enters the pre-condensation pipe 8 from the first air return pipe 72, and is subjected to pre-cooling condensation on high-temperature steam which is just led out from the retort barrel 2 in the vapor-liquid guide pipe 4; the pre-condensing pipe 8 raises the temperature of the gas and discharges the gas to the second gas return pipe 9, the gas is guided from the second gas return pipe 9 to the three-way valve 10, the second gas return pipe 9 can be communicated with the third gas return pipe 11 through the three-way valve 10 to guide the gas into the retort barrel 2, and the gas is circularly condensed, so that the resources are saved and the waste is avoided; the second gas return pipe 9 is communicated with the exhaust pipe 12 through the three-way valve 10 under the condition that the condensing box 6 is fully condensed, and the gas can be directly exhausted.

The principle and the implementation of the present invention are explained herein by using specific examples, and the above description of the embodiments is only used to help understand the method and the core idea of the present invention; meanwhile, for the general technical personnel in the field, according to the idea of the present invention, there are changes in the specific implementation and application scope, to sum up, the content of the present specification should not be understood as the limitation of the present invention.

Claims

1. The utility model provides a white spirit production distillation plant, includes end pot, its characterized in that: a retort barrel is arranged on the upper side of the bottom pot, an interlayer is arranged on the inner side of the side wall of the retort barrel, a cavity is formed between the interlayer and the side wall of the retort barrel, the lower end of the cavity is communicated with the inside of the retort barrel, a retort cover is arranged on the upper side of the retort barrel, a vapor-liquid guide pipe is connected with the retort cover, a centrifugal fan is arranged at the joint of the vapor-liquid guide pipe and the retort cover and guides fluid in the retort barrel and the retort cover into the vapor-liquid guide pipe, a condensing box is arranged at the tail end of the vapor-liquid guide pipe, a plurality of vertical heat exchange tubes are arranged at the upper part of the condensing box, the upper end and the lower end of each heat exchange tube are respectively connected with a distribution box and a liquid collecting box, the distribution box is connected with the vapor-liquid guide pipe, a heat exchange spiral pipe is connected to the lower side of the liquid collecting box, the tail, the other end of the pre-condensation pipe is connected with a second air return pipe, the second air return pipe is connected with a three-way valve, the three-way valve is also respectively connected with a third air return pipe and an exhaust pipe, and the third air return pipe is connected to the upper part of the retort barrel and communicated with the cavity.

2. The liquor production and distillation apparatus of claim 1, wherein: the lower end of the interlayer is provided with a gap with the bottom of the retort barrel.

3. The liquor production and distillation apparatus of claim 2, wherein: and the lower part and the upper part of the condensation box are respectively provided with a cooling medium inlet pipe and a cooling medium outlet pipe.

4. The liquor production and distillation apparatus of claim 3, wherein: and valves are arranged on the cooling medium inlet pipe, the cooling medium outlet pipe and the wine outlet pipe.

5. The liquor production and distillation apparatus of claim 4, wherein: the middle part of the separation box is connected with the heat exchange spiral pipe, and the upper part of the separation box is provided with a plurality of layers of filter screens.