CN211910391U - Passion fruit concentrated juice production facility - Google Patents
Passion fruit concentrated juice production facility Download PDFInfo
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- CN211910391U CN211910391U CN202020037024.5U CN202020037024U CN211910391U CN 211910391 U CN211910391 U CN 211910391U CN 202020037024 U CN202020037024 U CN 202020037024U CN 211910391 U CN211910391 U CN 211910391U
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- Prior art keywords
- fruit juice
- passion fruit
- liquid
- concentrated
- gas
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- 235000000370 Passiflora edulis Nutrition 0.000 title claims abstract description 50
- 244000288157 Passiflora edulis Species 0.000 title claims abstract description 50
- 235000011389 fruit/vegetable juice Nutrition 0.000 title claims abstract description 44
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 17
- 239000007788 liquid Substances 0.000 claims abstract description 70
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 45
- 235000015203 fruit juice Nutrition 0.000 claims abstract description 29
- 238000003860 storage Methods 0.000 claims abstract description 29
- 239000000126 substance Substances 0.000 claims abstract description 23
- 125000003118 aryl group Chemical group 0.000 claims abstract description 22
- 238000010438 heat treatment Methods 0.000 claims abstract description 20
- 238000009833 condensation Methods 0.000 claims abstract description 7
- 230000005494 condensation Effects 0.000 claims abstract description 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 14
- 229910001220 stainless steel Inorganic materials 0.000 claims description 8
- 239000010935 stainless steel Substances 0.000 claims description 8
- 229910052742 iron Inorganic materials 0.000 claims description 7
- 238000009413 insulation Methods 0.000 claims description 4
- 230000008676 import Effects 0.000 claims description 2
- 235000021579 juice concentrates Nutrition 0.000 claims 5
- 239000011229 interlayer Substances 0.000 claims 2
- 239000010410 layer Substances 0.000 claims 2
- 238000001816 cooling Methods 0.000 claims 1
- 239000004088 foaming agent Substances 0.000 claims 1
- 238000005057 refrigeration Methods 0.000 claims 1
- 238000009835 boiling Methods 0.000 abstract description 10
- 238000004821 distillation Methods 0.000 abstract description 7
- 230000008901 benefit Effects 0.000 abstract description 3
- 238000002425 crystallisation Methods 0.000 abstract description 3
- 230000008025 crystallization Effects 0.000 abstract description 3
- 238000001704 evaporation Methods 0.000 abstract description 3
- 230000008020 evaporation Effects 0.000 abstract description 3
- 238000000605 extraction Methods 0.000 abstract description 3
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- 238000010276 construction Methods 0.000 description 2
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- 208000007848 Alcoholism Diseases 0.000 description 1
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- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
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- 239000011574 phosphorus Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
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- 238000002360 preparation method Methods 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
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- 239000003053 toxin Substances 0.000 description 1
- 231100000765 toxin Toxicity 0.000 description 1
- 150000003722 vitamin derivatives Chemical class 0.000 description 1
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses the different characteristics of each component boiling point in the passion fruit juice of equipment utilization make the moisture of low boiling point and aromatic substance evaporate by heating and the distillation plant technical field of pure water and concentrated fruit juice is separated out in secondary condensation, relate to a passion fruit concentrated fruit juice production facility. Opening a valve of the liquid inlet, injecting the passion fruit juice into the liquid storage tank from the liquid inlet, then pumping the passion fruit juice into the concentration tank by the driving pump, heating and boiling the concentrated fruit juice by the heating pipe to obtain concentrated fruit juice, returning aromatic substance steam and partial steam into the concentrated fruit juice tank after passing through the gas-liquid separator and the primary condenser, and allowing the rest steam to flow into the condensed water storage tank after passing through the secondary condenser. The utility model discloses equipment has combined two kinds of unit operation of evaporation and condensation, compares with other means of separation like extraction, filtration crystallization etc. its advantage lies in not needing to use other solvents beyond the passion fruit juice to guarantee can not introduce new impurity.
Description
Technical Field
The utility model belongs to the technical field of utilize the different characteristics of each component boiling point in passion fruit juice to make the moisture of low boiling point and aromatic substance evaporate by heating and secondary condensation isolate the distillation plant of pure water and concentrated fruit juice, concretely relates to passion fruit concentrated fruit juice production facility.
Background
The passion fruit juice sold in the market is prepared by manually cutting passion fruit, pouring out pulp, adding drinking water and other flavoring agents, and is high in price, concentrated passion fruit juice does not exist in the market basically, and the concentrated passion fruit juice has huge market space and commercial development potential. The passion fruit juice contains 17 amino acids, is rich in 165 substances such as protein, fat, sugar, vitamins, calcium, phosphorus, iron, potassium, SOD enzyme, super fiber and the like which are beneficial to human bodies, is called as the king of VC (vitamin) in fruits, can promote the production of body fluid to quench thirst, refresh the mind, refresh the brain, relax the bowels, tonify the kidney, build the body, expel toxin, beautify the face, relieve alcoholism and protect the liver, has the effects of reducing cholesterol and hypertension and hyperglycemia, has the effects of treating oral ulcer, periodontitis and pharyngolaryngitis, has the effects of treating colitis and gastrointestinal diseases, regulates blood sugar, prevents diabetes, strengthens bones, and improves the immunity of human bodies.
Disclosure of Invention
The utility model aims at providing an utilize distillation technique to extract equipment of concentrated passion fruit juice, this equipment has combined two kinds of unit operations of evaporation and condensation, compares with other means of separation like extraction, filtration crystallization etc. its advantage lies in need not using other solvents beyond the passion fruit juice to guarantee can not introduce new impurity.
In order to achieve the above object, the utility model discloses the technical scheme that equipment adopted is: the utility model provides a concentrated fruit juice production facility of passion fruit, the device mainly includes inlet, concentrated jar, vapour and liquid separator, primary condenser, secondary condenser, vacuum pump, condensate water storage tank, concentrated fruit juice jar, heat source import and export, heating pipe, driving pump, liquid storage pot.
Opening a valve of the liquid inlet, injecting the passion fruit juice into the liquid storage tank from the liquid inlet, then pumping the passion fruit juice into the concentration tank by a driving pump, heating and boiling the concentrated fruit juice by the heating pipe to obtain concentrated fruit juice, returning aromatic substance steam and partial steam into the concentrated fruit juice tank after passing through the gas-liquid separator and the primary condenser, allowing the residual steam to flow into the condensed water storage tank after passing through the secondary condenser, and obtaining the liquid of the concentrated fruit juice tank as the total concentrated passion fruit juice obtained after the distillation.
The liquid inlet is a stainless steel faucet valve, the stainless steel faucet valve is welded at the top of the liquid storage tank, the liquid inlet valve is opened before the machine is started, and the other end of the liquid inlet is directly connected with the manufacturing and producing equipment of the passion fruit juice.
Pour into the liquid storage pot into the passion fruit juice from the inlet, the liquid outlet of liquid storage pot bottom connects gradually driving pump, concentrated jar through the pipe, and the passion fruit juice in the liquid storage pot is by external driving pump in concentrated jar, and concentrated jar is stainless steel intermediate layer insulation construction, places the foamer in the intermediate layer and keeps warm, and the driving pump is installed in the outer bottom of concentrated jar.
The passion fruit juice in the concentration tank generates a large amount of steam after being heated and boiled by the heating pipe, the heating pipe is a spiral hollow iron pipeline, the passion fruit juice in the concentration tank is heated by utilizing circulating hot water in the pipeline, and the spiral radiating area capable of increasing hot water is set to quickly improve the temperature of the passion fruit juice.
The heat source inlet and outlet are arranged on one side of the concentration tank, hot water flows in from the water inlet above and flows out from the water outlet below after flowing through the heating pipe, and the heat source inlet and outlet are also the beginning and the end of the heating pipe.
The passion fruit juice is heated and boiled to generate a large amount of steam, a vacuum pump is started, the steam is sucked into a gas-liquid separator through a top outlet of a concentration tank and an external communication conduit, the steam is mixed gas of aromatic substance steam and water steam, the gas temperature begins to drop in the gas-liquid separator, the aromatic substance steam is converged into liquid due to the fact that the boiling point of the aromatic substance is higher than that of water and flows to the bottom of the gas-liquid separator, and the water steam is still in a gas state.
The bottom of the gas-liquid separator is provided with a guide pipe communicated with the concentration tank, and the aromatic substance liquid gathered at the bottom of the gas-liquid separator flows back to the concentration tank along the guide pipe; under the action of a vacuum pump, water vapor still in a gas state is sucked into the primary condenser through a top outlet of the gas-liquid separator and the external communication conduit, the water vapor still contains a small part of aromatic substance gas, the small part of aromatic substance gas and the small part of water vapor are condensed to form liquid which is gathered at the bottom of the primary condenser, and the residual water vapor is sucked into the secondary condenser under the action of the vacuum pump.
When the gas temperature is reduced to below 100 ℃, the residual part of the water vapor is condensed into water and flows to the bottom of the secondary condenser, and flows into a condensed water storage tank along a conduit arranged at the outer bottom of the secondary condenser for storage.
The vacuum pump is connected with the top of secondary condenser through the stainless steel hollow tube with the screw, just start the vacuum pump when the passion fruit juice of concentration jar inside is heated to boiling 150 ℃, just close the vacuum pump after whole distillation process, two inlet valve that concentrate fruit juice jar will be opened to last step, concentrate fruit juice in the concentration jar flows in the concentrate fruit juice jar through one of them inlet valve, the aromatic substance liquid of condenser bottom is then through another inlet valve inflow concentrate fruit juice jar.
Spiral iron cooling water pipelines are arranged in the primary condenser and the secondary condenser, and cold water flows in the pipelines to reduce the temperature of steam in the condensers.
The utility model discloses equipment has following beneficial effect:
the utility model provides a concentrated fruit juice production facility of passion fruit, the utility model discloses equipment has combined two kinds of unit operation of evaporation and condensation, compares with other means of separation like extraction, filtration crystallization etc. its advantage lies in need not using other solvents beyond the passion fruit juice to guarantee can not introduce new impurity. And the water and electricity are saved, the operation is simple and convenient, the workers can easily use the hands, and the popularization is convenient.
Drawings
Fig. 1 is a schematic structural diagram of the present invention.
In the figure: 1 liquid inlet, 2 concentration tanks, 3 gas-liquid separators, 4 primary condensers, 5 secondary condensers, 6 vacuum pumps, 7 condensed water storage tanks, 8 concentrated juice tanks, 9 heat source inlets and outlets, 10 heating pipes, 11 driving pumps and 12 liquid storage tanks.
Detailed Description
The present invention will be further explained with reference to the accompanying drawings:
a passion fruit concentrated juice production device is shown in figure 1 and mainly comprises a liquid inlet 1, a concentration tank 2, a gas-liquid separator 3, a primary condenser 4, a secondary condenser 5, a vacuum pump 6, a condensed water storage tank 7, a concentrated juice tank 8, a heat source inlet and outlet 9, a heating pipe 10, a driving pump 11 and a liquid storage tank 12.
The principle is as follows: the passion fruit juice is injected into a liquid storage tank 12 from a liquid inlet 1, then the passion fruit juice is pumped into a concentration tank 2 by a driving pump 11, the concentrated fruit juice obtained after being heated and boiled by a heating pipe 10 flows into a concentrated fruit juice tank 8, aromatic substance steam and part of steam flow back into the concentrated fruit juice tank 8 after passing through a gas-liquid separator 3 and a primary condenser 4, the rest steam flows into a condensed water storage tank 7 after passing through a secondary condenser 5, and the liquid in the concentrated fruit juice tank 8 is the total concentrated passion fruit juice obtained after the distillation.
With passion fruit juice from inlet 1 injection liquid storage tank 12, the liquid outlet of liquid storage tank 12 bottom connects gradually driving pump 11, concentrated jar 2 through the pipe, and passion fruit juice in the liquid storage tank 12 is by external driving pump 11 pump income concentrated jar 2, and concentrated jar 2 is stainless steel intermediate layer insulation construction, places the foamer in the intermediate layer and keeps warm, and driving pump 11 installs the outer bottom at concentrated jar 2.
The passion fruit juice in the concentration tank 2 is heated and boiled by the heating pipe 10 to generate a large amount of steam, the heating pipe 10 is a spiral hollow iron pipeline, the passion fruit juice in the concentration tank 2 is heated by circulating hot water in the pipeline, and the spiral radiating area capable of increasing hot water is set to quickly improve the temperature of the passion fruit juice.
The heat source inlet and outlet 9 is installed at one side of the concentration tank 2, hot water flows in from the upper water inlet and flows out from the lower water outlet after flowing through the heating pipe 10, and the heat source inlet and outlet 9 is also the beginning and the end of the heating pipe 10.
The passion fruit juice is heated and boiled to generate a large amount of steam, a vacuum pump 6 is started, the steam is sucked into the gas-liquid separator 3 through an outlet at the top of the concentration tank 2 and an external communication conduit, the steam is mixed gas of aromatic substance steam and water steam, the temperature of the gas in the gas-liquid separator 3 begins to drop, the aromatic substance steam is converged into liquid due to the fact that the boiling point of the aromatic substance is higher than that of water, the aromatic substance steam flows to the bottom of the gas-liquid separator 3, and the water steam is still in a gas state.
The bottom of the gas-liquid separator 3 is provided with a conduit which is communicated with the concentration tank 2, and the aromatic substance liquid gathered at the bottom of the gas-liquid separator 3 flows back to the concentration tank 2 along the conduit.
Under the action of the vacuum pump 6, the water vapor still in a gas state is sucked into the primary condenser 4 through the top outlet of the gas-liquid separator 3 and an external communication conduit, the water vapor still contains a small part of aromatic substance gas, the small part of aromatic substance gas and the small part of water vapor are condensed to form liquid and are gathered at the bottom of the primary condenser 4, and the rest water vapor is sucked into the secondary condenser 5 under the action of the vacuum pump 6.
When the gas temperature is reduced to below 100 ℃, the residual part of the water vapor is condensed into water and flows to the bottom of the secondary condenser 5, and flows into a condensed water storage tank 7 along a conduit arranged at the outer bottom of the secondary condenser 5 for storage.
Spiral iron cooling water pipelines are arranged inside the primary condenser 4 and the secondary condenser 5, and cold water flows in the pipelines to reduce the temperature of steam in the condensers.
The foregoing is only a preferred embodiment of the present invention, and it should be noted that, for those skilled in the art, a plurality of improvements and decorations can be made without departing from the principle of the present invention, and these improvements and decorations should also be regarded as the protection scope of the present invention.
Claims (6)
1. The utility model provides a concentrated fruit juice production facility of passion fruit, includes inlet (1), concentrated jar (2), vapour and liquid separator (3), primary condenser (4), secondary condenser (5), vacuum pump (6), condensate storage tank (7), concentrated fruit juice jar (8), heat source import and export (9), heating pipe (10), driving pump (11), liquid storage tank (12), its characterized in that: the outlet end of the liquid inlet (1) is connected with the inlet end of a liquid storage tank (12), the outlet end of the liquid storage tank (12) is connected with the inlet end of a driving pump (11), the outlet end of the driving pump (11) is connected with the inlet end of a concentration tank (2), the gas outlet end of the concentration tank (2) is connected with the gas inlet end of a gas-liquid separator (3), and the liquid outlet end of the concentration tank (2) is connected with the concentrated juice inlet end of a concentrated juice tank (8) to form a juice concentration working line; the gas outlet end of the gas-liquid separator (3) is connected with the gas inlet end of the primary condenser (4), and the liquid outlet end of the primary condenser (4) is connected with the aromatic substance inlet end of the concentrated fruit juice tank (8) to form an aromatic substance condensation working line; the gas outlet end of the primary condenser (4) is connected with the gas inlet end of the secondary condenser (5), and the liquid outlet end of the secondary condenser (5) is connected with the inlet end of the condensed water storage tank (7), so that a condensation working line of the passion fruit juice evaporated water is formed.
2. The passion fruit juice concentrate production facility of claim 1, wherein: the other end of the liquid inlet (1) is directly connected with a manufacturing and producing device of passion fruit juice.
3. The passion fruit juice concentrate production facility of claim 1, wherein: the concentration tank (2) is of a stainless steel interlayer heat-insulation structure, and foaming agents are placed in the interlayer for heat insulation.
4. The passion fruit juice concentrate production facility of claim 1, wherein: the heating pipe (10) is a spiral hollow iron pipe, and heat exchange fins are processed on the inner side and the outer side of the pipe.
5. The passion fruit juice concentrate production facility of claim 1, wherein: the gas-liquid separator (3) is divided into an upper layer and a lower layer, and the middle is separated by a liquid baffle plate.
6. The passion fruit juice concentrate production facility of claim 1, wherein: spiral iron refrigeration water pipelines are arranged inside the primary condenser (4) and the secondary condenser (5), heat exchange fins are machined on the inner wall and the outer wall of each pipeline, and cooling circulating water flows in the pipelines.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020037024.5U CN211910391U (en) | 2020-01-09 | 2020-01-09 | Passion fruit concentrated juice production facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020037024.5U CN211910391U (en) | 2020-01-09 | 2020-01-09 | Passion fruit concentrated juice production facility |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN211910391U true CN211910391U (en) | 2020-11-13 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202020037024.5U Expired - Fee Related CN211910391U (en) | 2020-01-09 | 2020-01-09 | Passion fruit concentrated juice production facility |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN211910391U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113680086A (en) * | 2021-07-20 | 2021-11-23 | 青岛中万方能源科技有限公司 | Self-cleaning efficient concentrator |
-
2020
- 2020-01-09 CN CN202020037024.5U patent/CN211910391U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113680086A (en) * | 2021-07-20 | 2021-11-23 | 青岛中万方能源科技有限公司 | Self-cleaning efficient concentrator |
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Granted publication date: 20201113 |