CN210103876U - Yellow marshal apple essence extraction system - Google Patents
Yellow marshal apple essence extraction system Download PDFInfo
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- CN210103876U CN210103876U CN201920507785.XU CN201920507785U CN210103876U CN 210103876 U CN210103876 U CN 210103876U CN 201920507785 U CN201920507785 U CN 201920507785U CN 210103876 U CN210103876 U CN 210103876U
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Abstract
The utility model relates to an extraction system of yellow marshal apple essence, which is characterized in that the bottom of a vortex separator is communicated with the top through a pump PU02 to form external circulation, the top of the vortex separator is also communicated with a distillation tower, the top of the distillation tower is communicated with a condensing tower, the condensing tower is communicated with a warm water heat exchanger, and the warm water heat exchanger is communicated with a gradual cooling system; the bottom of the condensing tower is communicated with a distillation tower through a pump PU03, and the bottom of the distillation tower is simultaneously communicated with the tops of the distillation tower and a cooling tower through a pump PU06 to form external circulation; a passage between the condensing tower and the warm water heat exchanger is provided with a fragrance collecting and adjusting valve, and the washing tower is provided with a fragrance collecting and detecting device; an essence discharging adjusting valve is arranged at the discharging port; the temperature of the warm water is 30-45 ℃; circulating ice water is arranged in the gradual cooling system, and the temperature of the circulating ice water is 4-5 ℃. The utility model discloses be favorable to the extraction to yellow marshal apple essence, extraction efficiency is high, and the yellow marshal apple essence purity of extraction is high.
Description
Technical Field
The utility model relates to an extraction system of yellow marshal apple essence.
Background
Apple essence is various volatile fragrant components with pleasant smell formed in the ripening process of apples, and the volatile fragrant components exist in a certain proportion to form typical fragrance and taste of apples even a certain variety. The fruit juice can generate aroma in the processing process, the aroma becomes natural essence after deep processing, the essence contains nearly thousands of organic components such as enzyme, ester and the like, wherein the content of trans-2-hexenal is about 150 plus 200ppm, and the essence is a precious additive in the industries of high-grade food, beverage and cosmetics. Among them, the yellow marshal apple essence is widely pursued, so the process for extracting the yellow marshal apple essence is particularly important.
Disclosure of Invention
In order to extract yellow marshal apple essence with high efficiency, the utility model provides an extraction system of yellow marshal apple essence.
In order to achieve the purpose, the utility model adopts the following technical proposal:
an extraction system of yellow marshal apple essence comprises a vortex separator, wherein the bottom of the vortex separator is communicated with the top through a pump PU02 to form external circulation, the top of the vortex separator is also communicated with a distillation tower, the top of the distillation tower is communicated with a condensation tower, the condensation tower is communicated with a warm water heat exchanger, and the warm water heat exchanger is communicated with a gradual cooling system; the bottom of the condensing tower is communicated with a distillation tower through a pump PU03, and the bottom of the distillation tower is simultaneously communicated with the tops of the distillation tower and a cooling tower through a pump PU06 to form external circulation; the gradual cooling system comprises a primary separator, a secondary separator, a vacuum pump PU01, a primary heat exchanger, a secondary heat exchanger, a washing tower, a pump PU05, a discharge hole, a secondary heat exchanger, a pump PU04, a pump PU01, a pump PU05, a pump PU; a passage between the condensing tower and the warm water heat exchanger is provided with a fragrance collecting and adjusting valve, and the washing tower is provided with a fragrance collecting and detecting device; and an essence discharging adjusting valve is arranged at the discharging port.
The cooling system comprises a warm water circulating passage arranged outside the condensation tower, a temperature detection device arranged on a passage between the condensation tower and the warm water heat exchanger, and a warm water regulating valve arranged on the warm water circulating passage; the discharge gate still is provided with essence ejection of compact detection device. The PLC receives data from the temperature detection device, the aroma collection detection device and the essence discharge detection device, and controls the opening of the warm water regulating valve after processing and analysis so as to keep the cooling temperature constant; controlling the opening of the fragrance collecting adjusting valve to keep the fragrance amount (essence liquid level) temporarily stored in the washing tower stable; the essence discharge regulating valve is controlled to keep the essence discharge amount (essence flow) stable.
Further, the temperature of the warm water is 30-45 ℃; circulating ice water is arranged in the gradual cooling system, the temperature of the circulating ice water before entering the gradual cooling system is 4-5 ℃, and the temperature of the circulating ice water when being discharged out of the gradual cooling system is 8-9 ℃.
Further, the aroma collecting and detecting device is a liquid level transmitter for setting and detecting the liquid level of the washing tower.
Further, essence ejection of compact detection and control device is the turbine flowmeter who sets for and detect essence flow.
Further, the temperature detection device is a temperature sensor.
Further, a spraying device communicated with a pump PU02 is arranged at the top in the vortex separator; and spray devices communicated with PU06 are arranged at the tops of the distillation tower and the condensation tower.
Further, the distillation tower is designed to be of a laminar flow plate structure, and the surface of the laminar flow plate is provided with a punched convex hole. Thus greatly increasing the contact area of the condensed water and the fragrance volatilization.
Has the advantages that: the yellow marshal apple essence extraction system can extract natural yellow marshal apple essence, and the extracted yellow marshal apple essence is high in purity and high in extraction efficiency after being cooled by the gradual cooling system.
Drawings
FIG. 1 is a schematic diagram of an extraction system for yellow marshal apple essence;
in the figure, vortex separator 1, distillation column 2, condensing tower 3, warm water governing valve 4, temperature-detecting device 5, fragrance collection governing valve 6, warm water heat exchanger 7, first order separator 8, first order heat exchanger 9, second grade separator 10, vacuum pump PU 0111, second grade heat exchanger 12, washing tower 13, tertiary heat exchanger 14, turbine flowmeter 15, essence ejection of compact governing valve 16, liquid level changer 17, pump PU 0518, pump PU 0419, pump PU 0320, pump PU 0621, pump PU 0222.
Detailed Description
The present invention will be described in further detail with reference to the accompanying drawings and specific embodiments.
Example one
Fig. 1 shows an extraction system of yellow marshal apple essence, which comprises a vortex separator 1, wherein the bottom of the vortex separator 1 is communicated with the top through a pump PU0222 to form an external circulation, the top of the vortex separator 1 is also communicated with a distillation tower 2, the top of the distillation tower 2 is communicated with a condensation tower 3, the condensation tower 3 is communicated with a warm water heat exchanger 7, and the warm water heat exchanger 7 is communicated with a gradual cooling system; the bottom of the condensing tower 3 is communicated with the distillation tower 2 through a pump PU 0320, and the bottom of the distillation tower 2 is simultaneously communicated with the distillation tower 2 and the top of the cooling tower through a pump PU 0621 to form external circulation; the gradual cooling system comprises a primary separator 8, the top of the primary separator is communicated with a primary heat exchanger 9, the primary heat exchanger 9 is communicated with a secondary separator 10, the top of the secondary separator 10 is communicated with a vacuum pump PU 0111, the bottoms of the primary separator 8 and the secondary separator 10 are both communicated with a secondary heat exchanger 12 through a pump PU 0419, the secondary heat exchanger 12 and the vacuum pump PU 0111 are simultaneously communicated with a washing tower 13, the bottom of the washing tower 13 is communicated with a tertiary heat exchanger 14 through a pump PU 0518, and the top of the washing tower 13 and the tertiary heat exchanger 14 are simultaneously communicated with a discharge hole; a passage between the condensing tower 3 and the warm water heat exchanger 7 is provided with a fragrance collection regulating valve 6V204, and the washing tower 13 is provided with a fragrance collection detection device; and an essence discharging adjusting valve 16V205 is arranged at the discharging port.
The system for extracting the yellow marshal apple essence further comprises a controller PLC and a cooling temperature control system, wherein the cooling temperature control system comprises a warm water circulation passage arranged on the outer side of the condensation tower 3, a temperature detection device 5 arranged on a passage between the condensation tower 3 and the warm water heat exchanger 7, and a warm water regulating valve 4V203 arranged on the warm water circulation passage; the discharge gate still is provided with essence ejection of compact detection device. The PLC receives data from the temperature detection device 5, the aroma collection detection device and the essence discharge detection device, and controls the opening degree of the warm water regulating valve 4V203 after processing and analysis so as to keep the cooling temperature constant; the opening degree of the fragrance collection adjusting valve is controlled to be 6V204, so that the fragrance amount (essence liquid level) temporarily stored in the washing tower 13 is kept stable; the essence discharge adjusting valve 16V205 is controlled to keep the essence discharge amount (essence flow) stable.
The temperature of the warm water is 30-45 ℃; circulating ice water is arranged in the gradual cooling system, the temperature of the circulating ice water before entering the gradual cooling system is 4-5 ℃, and the temperature of the circulating ice water when being discharged out of the gradual cooling system is 8-9 ℃. As shown in fig. 1, the circulating ice water is divided into four paths, one path enters a washing tower 13, the other path enters a third-stage heat exchanger 14, the third path enters a second-stage heat exchanger 12, the fourth path enters a first-stage heat exchanger 9, and cooling water discharged from the washing tower 13 and the three and four paths of ice water are merged and enter the second-stage heat exchanger 12 and the first-stage heat exchanger 9.
The aroma collecting and detecting device is a liquid level transmitter 17LIC101 which is used for setting and detecting the liquid level of the washing tower 13. The essence ejection of compact detects controlling means for setting for and detect the turbine flowmeter 15FIC101 of essence flow. The temperature detection device 5 is a temperature sensor. A spraying device communicated with a pump PU0222 is arranged at the top in the vortex separator 1; and spray devices communicated with PU06 are arranged at the tops of the distillation tower 2 and the condensation tower 3.
The distillation tower 2 is designed to be of a laminar flow plate structure, and the surface of the laminar flow plate is provided with a punched convex hole. Thus greatly increasing the contact area of the condensed water and the fragrance volatilization.
Has the advantages that: the system for extracting the yellow marshal apple essence can extract natural yellow marshal apple essence, and the natural yellow marshal apple essence is gradually purified through the distillation tower 2, the cooling tower, the warm water heat exchanger 7 and the gradual cooling system, so that the extracted yellow marshal apple essence is high in purity and high in extraction efficiency; the cooling temperature is adjustable, and the discharge amount of the essence is stable and controllable.
Example two
Based on the extraction process of the yellow marshal apple essence extraction system in the embodiment, the embodiment comprises the following steps:
(1) squeezing;
(2) pre-concentration;
(3) killing the Pregabalin;
(4) carrying out gas-liquid separation on the turbid juice subjected to the killing of the propagules by a vortex type separator;
(5) the separated aroma-containing steam is sucked into the distillation tower 2 from the top of the vortex separator for evaporation; pumping the extracted cloudy juice from the bottom of the vortex separator by a pump PU0222, cooling, and performing enzymolysis;
(6) the aroma-containing steam with high concentration at the top of the distillation tower 2 enters a condensing tower 3 for condensation;
(7) the condensed aroma-containing steam enters a gradual cooling system for further condensation and cooling. Most of the aroma-containing steam in the condensing tower 3 is condensed into condensed water and is pumped back to the top of the distillation tower 2 by a pump PU 0320 to be used as water washing liquid, and a small part of the steam with high aroma concentration is sucked into a warm water heat exchanger 7 by a vacuum pump PU 0111 to be further condensed and cooled.
The temperature of the warm water is 30-45 ℃; circulating ice water is arranged in the gradual cooling system, the temperature of the circulating ice water before entering the gradual cooling system is 4-5 ℃, and the temperature of the circulating ice water when being discharged out of the gradual cooling system is 8-9 ℃. The temperature in the distillation tower 2 is 85-90 ℃.
The opening degree of the fragrance collection adjusting valve 6V204 is adjusted, so that the liquid level of the essence temporarily stored in the washing tower 13 is kept at 10-20%. The vacuum degree of the vacuum pump PU 0111 is-0.04-0.06. The pressure in the vortex separator is-0.065 to-0.050 MPa, and the temperature is 75 to 96 ℃. The essence discharge quantity is kept stable by adjusting the essence discharge adjusting valve 16V 205.
To sum up, the utility model discloses obvious beneficial effect does: aiming at yellow marshal apple, the utility model discloses, be favorable to the extraction of yellow marshal apple essence, extraction efficiency is high, and the yellow marshal apple essence purity of extraction is high, and essence fragrance quality is better.
Claims (5)
1. The system for extracting the yellow marshal apple essence is characterized by comprising a vortex separator, wherein the bottom of the vortex separator is communicated with the top of the vortex separator through a pump PU02 to form external circulation, the top of the vortex separator is also communicated with a distillation tower, the top of the distillation tower is communicated with a condensing tower, the condensing tower is communicated with a warm water heat exchanger, and the warm water heat exchanger is communicated with a gradual cooling system; the bottom of the condensing tower is communicated with a distillation tower through a pump PU03, and the bottom of the distillation tower is simultaneously communicated with the tops of the distillation tower and a cooling tower through a pump PU06 to form external circulation; the gradual cooling system comprises a primary separator, a secondary separator, a vacuum pump PU01, a primary heat exchanger, a secondary heat exchanger, a washing tower, a pump PU05, a discharge hole, a secondary heat exchanger, a pump PU04, a pump PU01, a pump PU05, a pump PU; a passage between the condensing tower and the warm water heat exchanger is provided with a fragrance collecting and adjusting valve, and the washing tower is provided with a fragrance collecting and detecting device; and an essence discharging adjusting valve is arranged at the discharging port.
2. The system for extracting yellow marshal apple essence according to claim 1, further comprising a controller PLC and a cooling temperature control system, wherein the cooling temperature control system comprises a warm water circulation passage arranged outside the condensation tower, a temperature detection device arranged on a passage between the condensation tower and the warm water heat exchanger, and a warm water regulating valve arranged on the warm water circulation passage; the discharge gate still is provided with essence ejection of compact detection device.
3. The system for extracting yellow marshal apple essence according to claim 2, wherein the aroma collection and detection device is a liquid level transmitter for setting and detecting the liquid level of the washing tower; the essence ejection of compact detects controlling means is for setting for and detecting the turbine flowmeter of essence flow.
4. The system for extracting yellow marshal apple essence according to claim 2, wherein a spraying device communicated with a pump PU02 is arranged at the top in the vortex separator; and spray devices communicated with PU06 are arranged at the tops of the distillation tower and the condensation tower.
5. The system for extracting yellow marshal apple essence according to claim 2, wherein the distillation tower is designed to be a laminar flow plate structure, and the surface of the laminar flow plate is provided with punched convex holes.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920507785.XU CN210103876U (en) | 2019-04-16 | 2019-04-16 | Yellow marshal apple essence extraction system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920507785.XU CN210103876U (en) | 2019-04-16 | 2019-04-16 | Yellow marshal apple essence extraction system |
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| Publication Number | Publication Date |
|---|---|
| CN210103876U true CN210103876U (en) | 2020-02-21 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201920507785.XU Expired - Fee Related CN210103876U (en) | 2019-04-16 | 2019-04-16 | Yellow marshal apple essence extraction system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109943413A (en) * | 2019-04-16 | 2019-06-28 | 宁夏吴忠市茂源天然果汁有限责任公司 | A kind of extraction system and its technique of Huang YUAN SHUAI apple essence |
-
2019
- 2019-04-16 CN CN201920507785.XU patent/CN210103876U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109943413A (en) * | 2019-04-16 | 2019-06-28 | 宁夏吴忠市茂源天然果汁有限责任公司 | A kind of extraction system and its technique of Huang YUAN SHUAI apple essence |
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