CN215694024U - Full-automatic closed hydrolysate deacidification facility - Google Patents
Full-automatic closed hydrolysate deacidification facility Download PDFInfo
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- CN215694024U CN215694024U CN202122228795.XU CN202122228795U CN215694024U CN 215694024 U CN215694024 U CN 215694024U CN 202122228795 U CN202122228795 U CN 202122228795U CN 215694024 U CN215694024 U CN 215694024U
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Abstract
The utility model discloses a full-automatic closed hydrolysate deacidification facility, relating to the field of hydrolysate processing facilities, which adopts a hollow oval tank body, a U-shaped base is respectively and longitudinally arranged at two ends of the bottom of the tank body, a cylindrical main shaft is transversely arranged below the tank body, a spiral propeller is arranged on the main shaft, the right side of the main shaft is connected with a graphite bearing at the right side surface of the tank body, the left side of the main shaft is connected with a central shaft of a speed regulating motor outside the left side surface of the tank body, a feeding pipe is arranged above the left side surface of the tank body, an F-shaped deacidification pipe is arranged in the middle of the right side surface of the tank body, the bottom of the right side face of the tank body is provided with a discharge pipe, when the yellow ginger mud and the hydrochloric acid enter the tank body, clear water is put into the tank body, the main shaft drives the propeller to rotate rapidly to stir, the stirring is finished and the stirring is static for 72 hours, waste acid above the stirring is discharged through the deacidification pipe, and then hydrolysate is discharged through the discharge pipe.
Description
Technical Field
The utility model discloses a full-automatic closed hydrolysate deacidification facility, and relates to the field of hydrolysate processing facilities.
Background
Hydrolysate, a saponin semi-finished product prepared from Curcuma rhizome. The turmeric needs to be washed, crushed, proportioned, acid boiled, deacidified, extracted and dried in the process of processing into hydrolysate. Most of the enterprises producing hydrolysates adopt a concrete pool during deacidification, yellow ginger mud and hydrochloric acid are required to be put into the concrete pool, then water is injected for stirring to deacidify, and finally acid water is pumped out and the hydrolysates are shoveled out. Therefore, a full-automatic closed hydrolysate deacidification facility is needed to replace the existing concrete pool deacidification.
Disclosure of Invention
The full-automatic closed hydrolysate deacidification facility overcomes the difficulties, adopts a hollow oval tank body, a U-shaped base is respectively and longitudinally arranged at two ends of the bottom of the tank body, a cylindrical main shaft is transversely arranged below the tank body, a spiral propeller is arranged on the main shaft, the right side of the main shaft is connected with a graphite bearing at the right side surface of the tank body, the left side of the main shaft is connected with a central shaft of a speed regulating motor outside the left side surface of the tank body, a feeding pipe is arranged above the left side surface of the tank body, an F-shaped deacidification pipe is arranged in the middle of the right side surface of the tank body, the bottom of the right side face of the tank body is provided with a discharge pipe, when the yellow ginger mud and the hydrochloric acid enter the tank body, clear water is put into the tank body, the main shaft drives the propeller to rotate rapidly to stir, the stirring is finished and the stirring is static for 72 hours, waste acid above the stirring is discharged through the deacidification pipe, and then hydrolysate is discharged through the discharge pipe.
A full-automatic closed hydrolysate deacidification facility comprises a base, a tank body, a main shaft, a propeller, a graphite bearing, a speed regulating motor, a discharge pipe, a discharge electric control valve, a first deacidification electric control valve, a second deacidification electric control valve, a deacidification pipe, an observation window, a feed pipe, a feed metering electric control valve, a water inlet pipe, a water inlet metering electric control valve, a control box, a power supply, a multi-way controller, a display screen and a power line;
the jar body is the cavity ellipse that the stainless steel was made, the both ends of jar body bottom have vertically set up the base of a U type respectively, the horizontal level in below of jar internal portion has set up the cylindrical main shaft that the stainless steel was made, the spiral propeller that the stainless steel was made has been set up on the main shaft, the top on main shaft the right side is connected with the ring shape graphite bearing that sets up in jar internal portion right flank below, rectangular glass observation window has been set up in the front of the jar body, the discharging pipe that the stainless steel was made has been set up to the bottom of jar body right flank, the entry position of discharging pipe has set up the circular ejection of compact electrically controlled valve that the stainless steel was made, the export of discharging pipe is connected with the drying-machine, the middle part of jar body right flank has set up the F type deacidification pipe that the stainless steel was made, the circular No. one deacidification electrically controlled valve that the stainless steel was made has been set up to the top entry position of deacidification pipe, the circular No. two deacidification electrically controlled valve that the stainless steel was made has been set up to the below entry position of deacidification pipe, The outlet of the deacidification pipe is connected with the waste acid neutralizing tank, a stainless steel feeding pipe is arranged above the left side surface of the tank body, a stainless steel round feeding metering electric control valve is arranged at the outlet of the feeding pipe, the inlet of the feeding pipe is connected with a centrifugal pump of the cooking tank, a water inlet pipe is arranged above the tank body, a stainless steel round water feeding metering electric control valve is arranged at the outlet of the water inlet pipe, and the inlet of the water inlet pipe is connected with a tap water pipe;
the speed regulating motor is transversely arranged below the left side surface of the tank body, and a stainless steel center shaft on the right side of the speed regulating motor penetrates through a rubber sealing ring on the tank body and extends into the tank body to be connected with the top end on the left side of the main shaft;
the control box is arranged on a power distribution cabinet of the assembly line, a display screen is arranged in front of the control box, and a power supply and a multi-path controller are arranged in the control box;
the power is connected with the multi-channel controller through a power line, and the multi-channel controller is connected with the display screen, the speed regulating motor, the discharging electric control valve, the first deacidification electric control valve, the second deacidification electric control valve, the feeding metering electric control valve and the water inlet metering electric control valve through the power line respectively.
Further, the adjustable speed motor, the discharging pipe, the deacidification pipe and the feeding pipe are arranged on two side faces of the tank body.
Has the advantages that: most of the enterprises producing hydrolysates adopt a concrete pool during deacidification, yellow ginger mud and hydrochloric acid are required to be put into the concrete pool, then water is injected for stirring to deacidify, and finally acid water is pumped out and the hydrolysates are shoveled out. A full-automatic closed hydrolysate deacidification facility adopts a hollow oval tank body, two ends of the bottom of the tank body are respectively and longitudinally provided with a U-shaped base, a cylindrical main shaft is transversely arranged below the inner part of the tank body, a spiral propeller is arranged on the main shaft, the right side of the main shaft is connected with a graphite bearing on the right side surface of the tank body, the left side of the main shaft is connected with a central shaft of a speed regulating motor outside the left side surface of the tank body, a feeding pipe is arranged above the left side surface of the tank body, an F-shaped deacidification pipe is arranged in the middle of the right side surface of the tank body, the bottom of the right side face of the tank body is provided with the discharging pipe, after the turmeric mud and the hydrochloric acid enter the tank body, clear water is put into the tank body, the main shaft drives the propeller to rotate rapidly to stir, the stirring is finished and stands still for 72 hours, waste acid above is discharged through the deacidification pipe, and then hydrolysate is discharged through the discharging pipe, so that the full-automatic closed hydrolysate deacidification effect is realized.
Drawings
FIG. 1 is a schematic diagram of a fully automatic closed hydrolysate deacidification facility;
FIG. 2 is a schematic circuit diagram of a fully automatic closed hydrolysate deacidification facility;
marked in the figure, the device comprises a base 1, a tank body 2, a main shaft 3, a propeller 4, a graphite bearing 5, a speed regulating motor 6, a discharge pipe 7, a discharge electric control valve 8, a first deacidification electric control valve 9, a second deacidification electric control valve 10, a deacidification pipe 11, an observation window 12, a feed pipe 13, a feed metering electric control valve 14, a water inlet pipe 15, a water inlet metering electric control valve 16, a control box 17, a power supply 18, a multi-way controller 19, a display screen 20 and a power line 21.
Detailed Description
The shape and construction of the present invention will now be described in detail with reference to the accompanying drawings and reference numerals:
a full-automatic closed hydrolysate deacidification facility is characterized by comprising a base 1, a tank body 2, a main shaft 3, a propeller 4, a graphite bearing 5, a speed regulating motor (AC380V/3-8kw)6, a discharge pipe 7, a discharge electric control valve (AC220V/3A)8, a first deacidification electric control valve (AC220V/3A)9, a second deacidification electric control valve (AC220V/3A)10, a deacidification pipe 11, an observation window 12, a feed pipe 13, a feed metering electric control valve (AC220V/5A)14, a feed pipe 15, a feed water metering electric control valve (AC220V/3A)16, a control box 17, a power supply (AC380V/40A)18, a multi-way controller (AC380V/40A, DC12V/5A)19, a display screen (DC12V/1A)20 and a power line 21;
the utility model discloses a dryer, including jar body 2, jar body 2 is the hollow ellipse that stainless steel made, the both ends of jar body 2 bottom have vertically set up the base 1 of a U type respectively, jar body 2 inside below horizontal level has set up cylindrical main shaft 3 that stainless steel made, the spiral propeller 4 that stainless steel made has been set up to the higher authority of main shaft 3, the top on main shaft 3 the right is connected with the ring shape graphite bearing 5 that sets up in jar body 2 inside right flank below, jar body 2 has set up rectangular glass observation window 12 in the front, jar body 2 right flank's bottom has set up discharging pipe 7 that stainless steel made, the entry position of discharging pipe 7 has set up circular ejection of compact electrically controlled valve 8 that stainless steel made, the export and the drying-machine of discharging pipe 7 are connected, jar body 2 right flank's middle part has set up F type deacidification pipe 11 that stainless steel made, the top entry position of deacidification pipe 11 has set up circular No. one electrically controlled valve 9 that stainless steel made, A circular second deacidification electric control valve 10 made of stainless steel is arranged at an inlet position below the deacidification pipe 11, an outlet of the deacidification pipe 11 is connected with a waste acid neutralizing tank, a feeding pipe 13 made of stainless steel is arranged above the left side surface of the tank body 2, a circular feeding metering electric control valve 14 made of stainless steel is arranged at an outlet position of the feeding pipe 13, an inlet of the feeding pipe 13 is connected with a centrifugal pump of the cooking tank, a water inlet pipe 15 is arranged on the tank body 2, a circular water feeding metering electric control valve 16 made of stainless steel is arranged at an outlet position of the water inlet pipe 15, and an inlet of the water inlet pipe 15 is connected with a tap water pipe;
the speed regulating motor 6 is transversely arranged below the left side surface of the tank body 2, and a stainless steel center shaft on the right side of the speed regulating motor 6 penetrates through a rubber sealing ring on the upper surface of the tank body 2 to extend into the tank body 2 and be connected with the top end on the left side of the main shaft 3;
the control box 17 is arranged on a power distribution cabinet of the assembly line, a display screen 20 is arranged in front of the control box 17, and a power supply 18 and a multi-channel controller 19 are arranged inside the control box;
the power supply 18 is connected with the multi-channel controller 19 through a power line 21, and the multi-channel controller 19 is respectively connected with the display screen 20, the speed regulating motor 6, the discharging electric control valve 8, the first deacidification electric control valve 9, the second deacidification electric control valve 10, the feeding metering electric control valve 14 and the water inlet metering electric control valve 16 through the power line 21.
Further, the speed regulating motor 6, the discharge pipe 7, the deacidification pipe 11 and the feed pipe 13 are arranged on two side surfaces of the tank body 2.
When the full-automatic closed hydrolysate deacidification facility is used, a worker turns on the power supply 18 and clicks a working key on the display screen 20, at the moment, the multi-path controller 19 simultaneously controls the feeding metering electric control valve 14 and the water inlet metering electric control valve 16 to be turned on, the feeding metering electric control valve 14 starts to meter the amount of the turmeric mud and the hydrochloric acid entering the tank body 2 until the amount reaches 3/5 of the total volume inside the tank body 2 and transmits data to the multi-path controller 19, the feeding metering electric control valve 14 is turned off after the multi-path controller 19 receives the data that the amount of the turmeric mud and the hydrochloric acid reaches the upper limit, at the same time, the water inlet metering electric control valve 16 starts to meter the amount of the clear water entering the tank body 2 until the amount reaches 3/10 of the total volume inside the tank body 2 and transmits the data to the multi-path controller 19, and the multi-path controller 19 closes the water inlet metering electric control valve 16 after the amount of the clear water reaches the upper limit, at the moment, the multi-path controller 19 controls the speed regulating motor 6 to drive the propeller 4 to rotate clockwise and rotate rapidly to fully dilute the yellow ginger mud, the hydrochloric acid and the clear water through the main shaft 3, the stirring is stopped after 20-40min, after 48h, the yellow ginger mud in the tank body 2 becomes hydrolysate and is deposited below the tank body 2, in the process, workers check the precipitation condition of the hydrolysate through the observation window 12 to adjust the precipitation time in a proper amount, at the moment, the multi-path controller 19 controls the first deacidification electric control valve 9 to be opened, the waste acid above the tank body 2 is put into the waste acid neutralization tank through the deacidification pipe 11, after 2h, the multi-path controller 19 controls the first deacidification electric control valve 9 to be closed, after 72h, the multi-path controller 19 controls the second deacidification electric control valve 10 to be opened, the waste acid in the middle part of the tank body 2 is put into the waste acid neutralization tank through the deacidification pipe 11, and after 2h, the multi-path controller 19 controls the second deacidification electric control valve 10 to be closed, at the moment, the multi-channel controller 19 controls the discharging electric control valve 8 to be opened, controls the speed regulating motor 6 to drive the propeller 3 to rotate anticlockwise slowly, feeds the hydrolysate into the dryer through the discharging electric control valve 8 and the discharging pipe 7, and controls the discharging electric control valve 8 to be closed after 1 hour.
The above-mentioned non-detailed description is prior art.
Claims (2)
1. A full-automatic closed hydrolysate deacidification facility is characterized by comprising a base, a tank body, a main shaft, a propeller, a graphite bearing, a speed regulating motor, a discharge pipe, a discharge electric control valve, a first deacidification electric control valve, a second deacidification electric control valve, a deacidification pipe, an observation window, a feed pipe, a feed metering electric control valve, a water inlet pipe, a water inlet metering electric control valve, a control box, a power supply, a multi-way controller, a display screen and a power line;
the jar body is the cavity ellipse that the stainless steel was made, the both ends of jar body bottom have vertically set up the base of a U type respectively, the horizontal level in below of jar internal portion has set up the cylindrical main shaft that the stainless steel was made, the spiral propeller that the stainless steel was made has been set up on the main shaft, the top on main shaft the right side is connected with the ring shape graphite bearing that sets up in jar internal portion right flank below, rectangular glass observation window has been set up in the front of the jar body, the discharging pipe that the stainless steel was made has been set up to the bottom of jar body right flank, the entry position of discharging pipe has set up the circular ejection of compact electrically controlled valve that the stainless steel was made, the export of discharging pipe is connected with the drying-machine, the middle part of jar body right flank has set up the F type deacidification pipe that the stainless steel was made, the circular No. one deacidification electrically controlled valve that the stainless steel was made has been set up to the top entry position of deacidification pipe, the circular No. two deacidification electrically controlled valve that the stainless steel was made has been set up to the below entry position of deacidification pipe, The outlet of the deacidification pipe is connected with the waste acid neutralizing tank, a stainless steel feeding pipe is arranged above the left side surface of the tank body, a stainless steel round feeding metering electric control valve is arranged at the outlet of the feeding pipe, the inlet of the feeding pipe is connected with a centrifugal pump of the cooking tank, a water inlet pipe is arranged above the tank body, a stainless steel round water feeding metering electric control valve is arranged at the outlet of the water inlet pipe, and the inlet of the water inlet pipe is connected with a tap water pipe;
the speed regulating motor is transversely arranged below the left side surface of the tank body, and a stainless steel center shaft on the right side of the speed regulating motor penetrates through a rubber sealing ring on the tank body and extends into the tank body to be connected with the top end on the left side of the main shaft;
the control box is arranged on a power distribution cabinet of the assembly line, a display screen is arranged in front of the control box, and a power supply and a multi-path controller are arranged in the control box;
the power is connected with the multi-channel controller through a power line, and the multi-channel controller is connected with the display screen, the speed regulating motor, the discharging electric control valve, the first deacidification electric control valve, the second deacidification electric control valve, the feeding metering electric control valve and the water inlet metering electric control valve through the power line respectively.
2. A fully automatic closed deacidification facility for hydrolysates as claimed in claim 1, wherein the speed regulating motor, the discharge pipe, the deacidification pipe and the feed pipe are arranged on two side surfaces of the tank body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122228795.XU CN215694024U (en) | 2021-09-14 | 2021-09-14 | Full-automatic closed hydrolysate deacidification facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122228795.XU CN215694024U (en) | 2021-09-14 | 2021-09-14 | Full-automatic closed hydrolysate deacidification facility |
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| Publication Number | Publication Date |
|---|---|
| CN215694024U true CN215694024U (en) | 2022-02-01 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202122228795.XU Active CN215694024U (en) | 2021-09-14 | 2021-09-14 | Full-automatic closed hydrolysate deacidification facility |
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| CN (1) | CN215694024U (en) |
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2021
- 2021-09-14 CN CN202122228795.XU patent/CN215694024U/en active Active
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