CN220618863U - Disc type condenser - Google Patents

Disc type condenser Download PDF

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Publication number
CN220618863U
CN220618863U CN202321632575.6U CN202321632575U CN220618863U CN 220618863 U CN220618863 U CN 220618863U CN 202321632575 U CN202321632575 U CN 202321632575U CN 220618863 U CN220618863 U CN 220618863U
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Prior art keywords
fin
condenser
pipe
condensation
disc
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CN202321632575.6U
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Chinese (zh)
Inventor
王玉平
杨番平
高慧连
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Shanxi Yimen Sanjinshi Liquor Industry Co ltd
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Shanxi Yimen Sanjinshi Liquor Industry Co ltd
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Abstract

The utility model relates to a disc type condenser, wherein a primary disc type condensation bag (1) is arranged at an opening hole at the upper part of a secondary fin condenser (4), a distilled liquor inlet pipe (2) is arranged at a surface opening hole of the primary disc type condensation bag (1), two sides of the secondary fin condenser (4) are respectively provided with radiating fins (3) through a bracket and more than two pipelines, the radiating fins (3) are fixedly provided with cooling fans (5) through screws, and a discharging pipe (6) is arranged at a through hole at the lower part surface of the secondary fin condenser (4); the utility model can continuously condense white spirit, can continuously produce white spirit by a plurality of distillation pots, and effectively improves the production efficiency of winery.

Description

Disc type condenser
Technical Field
The utility model relates to white spirit production equipment, in particular to a disc type condenser.
Background
In the processing process of white spirit, qualified white spirit can be brewed by crushing raw materials, steaming, gelatinizing, mixing with fermented grains, entering a cellar, grasping the temperature of the product, distilling, picking up the white spirit and ageing. The fermented grains after fermentation contain extremely complex components. The active ingredients of alcohol, water, esters, acids, etc. in the fermented grains are evaporated into steam by distillation, and then cooled to obtain the white spirit. Distillation is therefore an important part of brewing. At present, effective components such as alcohol, esters, acids and the like are condensed into liquid state from steam through a condenser, the existing condenser is mainly made of stainless steel, a cold water tank and a pipeline for cooling are arranged in the existing condenser, so that the effective components such as alcohol, water, esters, acids and the like in a steam state are condensed into liquid state again, but the existing condenser cannot be discharged in time after absorbing a large amount of heat due to the fact that an internal cooling medium of the existing condenser is poor in condensation effect, and the existing condenser needs to wait for natural cooling, so that the production efficiency of a winery is reduced, and the economic benefits of enterprises are affected. At present, the utility model with the patent number of CN207175906U discloses a water injection device for a distilled water seal tank of white spirit, in particular relates to a water injection device for a distilled water seal tank of white spirit, which comprises a steamer pot and a condenser, wherein a steam passing cylinder is communicated between the steamer pot and the condenser, a steamer pot water seal tank is arranged at the joint of the steamer pot and the steam passing cylinder, a condenser water seal tank is arranged between the condenser and the steam passing cylinder, a water injection pipe is arranged on the steam passing cylinder, openings are respectively arranged at two ends of the water injection pipe and are respectively aligned with the steamer pot water seal tank and the condenser water seal tank, a branch pipe with a water valve is communicated on the water injection pipe, a water inlet pipe is communicated with the branch pipe, and a water pump is communicated with the water inlet pipe. The utility model improves the production efficiency of white spirit, and has simple structure, convenience and practicability. However, the solution of this application still does not solve the problem of poor condensation effect after long-time use, and the use of the solution is inconvenient because the solution needs a long time before each use.
Disclosure of Invention
Aiming at the problems in the prior art, the utility model provides the disc type condenser which can continuously condense white spirit, and a plurality of distillation pots can continuously produce the white spirit, so that the production efficiency of a winery is effectively improved.
In order to achieve the above purpose, the utility model relates to a disc type condenser, which comprises a primary disc type condensation package, a disc type condensation pipe, a primary cooling liquid cavity, a distilled liquor inlet pipe, cooling fins, a secondary fin condenser, a secondary condensation fin, a secondary cooling liquid cavity, a collecting box, a cooling fan and a discharging pipe, wherein a primary disc type condensation package is arranged at an opening hole at the upper part of the secondary fin condenser, the distilled liquor inlet pipe is arranged at the surface of the primary disc type condensation package, the cooling fins are respectively arranged at two sides of the secondary fin condenser through a bracket and more than two pipelines, the cooling fan is fixedly arranged on the cooling fins through screws, and the discharging pipe is arranged at the surface of the lower part of the secondary fin condenser; the inside of a first-stage cooling liquid cavity inside a first-stage disc type condensation bag is provided with a disc type condensation pipe through a bracket, the inside of a second-stage cooling liquid cavity inside a second-stage fin condenser is provided with a second-stage condensation fin through a bracket, the first-stage cooling liquid cavity and the second-stage cooling liquid cavity are communicated with each other, one end of the disc type condensation pipe is connected with a distilled liquor steam inlet pipe, the other end of the disc type condensation pipe is connected with a condensation pipe in the second-stage condensation fin, the lower opening of the condensation pipe in the second-stage condensation fin is connected with a collecting box through a pipeline, the collecting box is provided with a trash discharging pipe, the top end of the trash discharging pipe is higher than the upper surface of the disc type condensation pipe, a water inlet pipe at the lower part of the heat radiating fin penetrates through a second-stage fin condenser shell to be connected with the second-stage cooling liquid cavity, and a water outlet pipe at the upper part of the heat radiating fin penetrates through the first-stage disc type condensation bag shell to be connected with the first-stage cooling liquid cavity; the water outlet pipe of the radiating fin is provided with a water pump.
As a further improvement scheme of the utility model, the pipeline inlet inside the secondary condensation fin is bifurcated into a plurality of coils, and the outlet is converged into a water outlet pipe.
As a further improvement of the utility model, the coils in the two-stage condensation fins are all provided with tesla valves.
As a further improvement of the utility model, the surface of the disc type condensing tube is provided with fins.
As a further improvement of the utility model, the radiating fins can be replaced by a refrigerator.
As a further improvement scheme of the utility model, the upper part of the collecting box is provided with a serial pipeline, and the serial pipeline is provided with a valve.
By means of the scheme, the utility model has at least the following advantages: compared with a conventional condenser, the space for condensing the white spirit by using the condensing equipment is greatly expanded by using a small space through the disc type condensing pipe and the secondary condensing fins, and the refrigerants in the primary cooling liquid cavity and the secondary cooling liquid cavity can be quickly cooled through the radiating fins, so that the equipment can continuously condense the white spirit by using a plurality of distillation pots, the white spirit can be continuously produced, the production efficiency of a winery is effectively improved, and the environment-friendly benefit and the economic benefit are remarkable.
Drawings
FIG. 1 is a schematic perspective view of a tray condenser;
FIG. 2 is a front cross-sectional view of a disc condenser;
in the figure: 1. the device comprises a primary disc type condensation bag, a disc type condensation pipe, a primary cooling liquid cavity, a distilled liquor inlet pipe, a cooling fin, a secondary fin condenser, a cooling fan, a discharging pipe and a cooling fin, wherein the primary disc type condensation bag, the disc type condensation pipe, the primary cooling liquid cavity, the cooling fin and the cooling fin are sequentially arranged in the primary cooling liquid cavity, the cooling fin and the cooling fin.
Detailed Description
The following description of the embodiments of the present utility model will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present utility model, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
In the description of the present utility model, it should be noted that the azimuth or positional relationship indicated by the terms "center", "up", "down", "left", "right", "vertical", "horizontal", "inside", "outside", etc. are based on the azimuth or positional relationship shown in the drawings, are merely for convenience of describing the present utility model and simplifying the description, and do not indicate or imply that the apparatus or elements referred to must have a specific azimuth, be constructed and operated in a specific azimuth, and thus should not be construed as limiting the present utility model. Furthermore, in the description of the present specification, the terms "first," "second," and the like are used for descriptive purposes only and are not to be construed as indicating or implying a relative importance or implying a number of technical features being indicated. Thus, a feature defining "a first" or "a second" may explicitly or implicitly include at least one such feature. In the description of the present application, the meaning of "plurality" is at least two, such as two, three, etc., unless explicitly defined otherwise.
As shown in fig. 1 and 2, the disc condenser comprises a first-stage disc condensation package 1, a disc condensation pipe 1-1, a first-stage cooling liquid cavity 1-2, a distilled liquor steam inlet pipe 2, cooling fins 3, a second-stage fin condenser 4, a second-stage condensation fin 4-1, a second-stage cooling liquid cavity 4-2, a collecting box 4-3, a cooling fan 5 and a discharging pipe 6, wherein the first-stage disc condensation package 1 is arranged at an opening hole at the upper part of the second-stage fin condenser 4, the distilled liquor steam inlet pipe 2 is arranged at an opening hole at the surface of the first-stage disc condensation package 1, the cooling fins 3 are respectively arranged at two sides of the second-stage fin condenser 4 through brackets and more than two pipelines, the cooling fan 5 is fixedly arranged on the cooling fins 3 through screws, and the discharging pipe 6 is arranged at an opening hole at the lower part surface of the second-stage fin condenser 4; the inside of a first-stage cooling liquid cavity 1-2 inside a first-stage disc type condensation bag 1 is provided with a disc type condensation pipe 1-1 through a bracket, the inside of a second-stage cooling liquid cavity 4-2 inside a second-stage fin condenser 4 is provided with a second-stage condensation fin 4-1 through a bracket, the first-stage cooling liquid cavity 1-2 and the second-stage cooling liquid cavity 4-2 are communicated with each other, one end of the disc type condensation pipe 1-1 is connected with a distilled liquor steam inlet pipe 2, the other end is connected with a condensation pipe in the second-stage condensation fin 4-1, the lower opening of the condensation pipe in the second-stage condensation fin 4-1 is connected with a collecting box 4-3 through a pipeline, the collecting box 4-3 is provided with a trash discharge pipe, the top end of the trash discharge pipe is higher than the upper surface of the disc type condensation pipe 1-1, a water inlet pipe at the lower part of the heat dissipation fin 3 penetrates through the outer shell of the second-stage fin condenser 4 to be connected with the second-stage cooling liquid cavity 4-2, and a water outlet pipe at the upper part of the heat dissipation fin 3 penetrates through the outer shell of the first-stage disc type condensation bag 1 to be connected with the first-stage cooling liquid cavity 1-2; the water outlet pipe of the heat radiation fin 3 is provided with a water pump.
In order to improve the condensation efficiency, as a further improvement scheme of the utility model, the pipeline inlet inside the secondary condensation fin 4-1 is branched into a plurality of coils, and the outlet is converged into a water outlet pipe. In order to make the steam move more slowly in the secondary condensing fins 4-1 and cool it further, as a further improvement of the utility model, a plurality of coils in the secondary condensing fins 4-1 are provided with tesla valves. In order to improve the heat exchange efficiency, as a further improvement scheme of the utility model, the surface of the disc type condensation tube 1-1 is provided with fins. In order to further improve the condensation efficiency of the device, as a further improvement scheme of the utility model, the heat radiation fins 3 can be replaced by a refrigerator. In order to enable the equipment to be connected in series in multiple stages to further improve the continuous working capacity, as a further improvement of the utility model, the upper part of the collecting box 4-3 is provided with a series pipeline, and the series pipeline is provided with a valve.
In use, a disc condenser is installed, and a plurality of distillation pans are connected to the distilled liquor inlet pipe 2 through pipelines, and valves are arranged on the pipelines. The utility model discloses a water injection device for a distilled water seal tank of white spirit, which is characterized by comprising a steamer pot and a condenser, wherein a steam drum is communicated between the steamer pot and the condenser, a steamer pot water seal tank is arranged at the joint of the steamer pot and the steam drum, a condenser water seal tank is arranged between the condenser and the steam drum, a water injection pipe is arranged on the steam drum, openings are respectively arranged at two ends of the water injection pipe and are respectively aligned with the steamer pot water seal tank and the condenser water seal tank, a branch pipe with a water valve is communicated on the water injection pipe, a water inlet pipe is communicated with the branch pipe, and a water pump is communicated with the water inlet pipe. The utility model improves the production efficiency of white spirit, and has simple structure, convenience and practicability. However, the solution of this application still does not solve the problem of poor condensation effect after long-time use, and the use of the solution is inconvenient because the solution needs a long time before each use. The space for condensing the white spirit by the condensing equipment is greatly expanded by the disc type condensing pipe 1-1 and the secondary condensing fins 4-1, and the cooling medium in the primary cooling liquid cavity 1-2 and the secondary cooling liquid cavity 4-2 can be quickly radiated by the radiating fins 3, so that the equipment can continuously condense the white spirit by a plurality of distillation pots, the white spirit can be continuously produced, the production efficiency of a winery is effectively improved, and the utility model has remarkable environmental protection benefit and economic benefit.
When the utility model is used, the concrete work is as follows:
when in use, a plurality of stills are connected to the distilled liquor steam inlet pipe 2 through pipelines, when one stills starts to work, other stills pipelines are closed by valves, steam enters the primary disc type condensation bag 1 through the distilled liquor steam inlet pipe 2, and is condensed under the action of the refrigerant in the primary cooling liquid cavity 1-2 when passing through the disc type condensation pipe 1-1, because the disc type condensation pipe 1-1 has smaller volume, the length of the cold energy pipe is greatly prolonged through the disc type pipeline with a circular structure, the heat exchange speed of the refrigerant in the disc type condensation pipe 1-1 and the primary cooling liquid cavity 1-2 is increased through the fins, so that the steam can be cooled more quickly when being condensed for a longer distance, and most of steam is changed into white spirit after passing through the disc type condensation pipe 1-1, at this time, the part of the steam and the white spirit continuously descends to the secondary fin condenser 4 under the action of the subsequent vapor pressure, branches into a plurality of coils in the secondary condensation fins 4-1 in the secondary fin condenser 4, and further cools the pipeline which is discharged and converged into a single pipe orifice at the outlet, and the secondary condensation fins 4-1 can accelerate the heat exchange speed with the refrigerant in the secondary cooling liquid cavity 4-2 through the fins, so that the white spirit and the steam mixture can be further cooled into the white spirit, when the primary disc type condensation package 1 and the secondary fin condenser 4 work, the cooling fins 3 continuously pump out the refrigerant in the primary cooling liquid cavity 1-2 and the secondary cooling liquid cavity 4-2 and cool the refrigerant in the primary cooling liquid cavity 1-2 and the secondary cooling liquid cavity 4-2, so that the refrigerant in the equipment is always kept at a colder position, so that the device can continuously condense the white spirit, and the white spirit which is condensed is discharged through the discharging pipe 6.
In the description of the present specification, a description referring to the terms "one embodiment," "some embodiments," "examples," "specific examples," or "some examples," etc., means that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example of the present application. In this specification, schematic representations of the above terms are not necessarily directed to the same embodiment or example. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples. Furthermore, the different embodiments or examples described in this specification and the features of the different embodiments or examples may be combined and combined by those skilled in the art without contradiction.
Although embodiments of the present application have been shown and described above, it will be understood that the above embodiments are illustrative and not to be construed as limiting the application, and that variations, modifications, alternatives, and variations may be made to the above embodiments by one of ordinary skill in the art within the scope of the application.

Claims (6)

1. The utility model provides a disc condenser, includes second grade fin condenser (4) and discharging pipe (6), its characterized in that, second grade fin condenser (4) upper portion open hole installation one-level disc condensation package (1), one-level disc condensation package (1) surface open hole installation distilled liquor admission pipe (2), second grade fin condenser (4) both sides are respectively through support and more than two pipeline installation cooling fin (3), cooling fin (3) pass through screw fixed mounting cooling fan (5), second grade fin condenser (4) lower part surface open hole installation discharging pipe (6); the inside of a primary cooling liquid cavity (1-2) at the inner side of a primary disc type condensation bag (1) is provided with a disc type condensation pipe (1-1) through a bracket, the inside of a secondary cooling liquid cavity (4-2) at the inner side of a secondary fin condenser (4) is provided with a secondary condensation fin (4-1) through a bracket, the primary cooling liquid cavity (1-2) and the secondary cooling liquid cavity (4-2) are communicated with each other, one end of the disc type condensation pipe (1-1) is connected with a distilled liquor inlet pipe (2), the other end of the disc type condensation pipe is connected with a condensation pipe in the secondary condensation fin (4-1), the lower opening of the condensation pipe in the secondary condensation fin (4-1) is connected with a collecting box (4-3) through a pipeline, the top end of the collecting box (4-3) is higher than the upper surface of the disc type condensation pipe (1), a water inlet pipe at the lower part of the heat dissipation fin (3) penetrates through a shell of the secondary fin condenser (4) to be connected with the secondary cooling liquid cavity (4-2), and a water outlet pipe at the upper part of the fin (3) penetrates through the primary condensation bag (1) to be connected with the disc type cooling liquid cavity (1-2); the water outlet pipe of the heat radiation fin (3) is provided with a water pump.
2. A disc condenser according to claim 1, wherein the inlet of the tube inside the secondary condensing fin (4-1) is bifurcated into a plurality of coils and the outlet is convergent into a water outlet tube.
3. A disc condenser according to claim 2, characterized in that the coils in the secondary condenser fins (4-1) are provided with tesla valves.
4. A disc condenser according to claim 1, wherein the surface of the disc condenser tube (1-1) is provided with fins.
5. A disc condenser according to claim 1 or 4, characterized in that the heat radiation fins (3) are exchangeable for a refrigerator.
6. A disc condenser according to claim 1, characterized in that the upper part of the collecting tank (4-3) is provided with a series connection of pipes, which are provided with valves.
CN202321632575.6U 2023-06-26 2023-06-26 Disc type condenser Active CN220618863U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202321632575.6U CN220618863U (en) 2023-06-26 2023-06-26 Disc type condenser

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202321632575.6U CN220618863U (en) 2023-06-26 2023-06-26 Disc type condenser

Publications (1)

Publication Number Publication Date
CN220618863U true CN220618863U (en) 2024-03-19

Family

ID=90215316

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202321632575.6U Active CN220618863U (en) 2023-06-26 2023-06-26 Disc type condenser

Country Status (1)

Country Link
CN (1) CN220618863U (en)

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