CN220801964U - Vacuum distillation concentration device for abalone feed liquid - Google Patents
Vacuum distillation concentration device for abalone feed liquid Download PDFInfo
- Publication number
- CN220801964U CN220801964U CN202322417322.3U CN202322417322U CN220801964U CN 220801964 U CN220801964 U CN 220801964U CN 202322417322 U CN202322417322 U CN 202322417322U CN 220801964 U CN220801964 U CN 220801964U
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- tank
- vacuum distillation
- abalone feed
- concentration device
- concentration
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- 239000007788 liquid Substances 0.000 title claims abstract description 34
- 238000005292 vacuum distillation Methods 0.000 title claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 33
- 238000009413 insulation Methods 0.000 claims abstract description 15
- 238000007789 sealing Methods 0.000 claims abstract description 12
- 238000005485 electric heating Methods 0.000 claims abstract description 8
- 239000000523 sample Substances 0.000 claims abstract description 6
- 238000003756 stirring Methods 0.000 claims description 16
- 239000010410 layer Substances 0.000 claims description 14
- 238000004321 preservation Methods 0.000 claims description 8
- 238000004140 cleaning Methods 0.000 claims description 6
- 239000011521 glass Substances 0.000 claims description 4
- 239000011229 interlayer Substances 0.000 claims description 4
- 238000009434 installation Methods 0.000 claims description 2
- 238000004821 distillation Methods 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 4
- 238000001704 evaporation Methods 0.000 abstract description 3
- 230000008020 evaporation Effects 0.000 abstract description 3
- 238000005086 pumping Methods 0.000 abstract description 3
- 238000011084 recovery Methods 0.000 abstract description 2
- 238000009833 condensation Methods 0.000 abstract 1
- 230000005494 condensation Effects 0.000 abstract 1
- 239000012141 concentrate Substances 0.000 description 4
- 239000012530 fluid Substances 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 238000007599 discharging Methods 0.000 description 2
- 108090000765 processed proteins & peptides Proteins 0.000 description 2
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000009849 deactivation Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 210000001503 joint Anatomy 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 235000013372 meat Nutrition 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 230000000007 visual effect Effects 0.000 description 1
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a vacuum distillation concentration device for abalone feed liquid, which comprises a concentration tank, a condenser, a receiving tank and a water tank which are sequentially connected through pipelines, wherein the concentration tank comprises an oil heat insulation layer, an inner container positioned in the oil heat insulation layer and a sealing cover detachably arranged above the inner container, an electric heating pipe is arranged on the inner side of the oil heat insulation layer, a feed inlet is arranged on the sealing cover, a temperature control probe and a discharge outlet are arranged at the bottom of the inner container, a driving mechanism is arranged at the top of the sealing cover, a stirrer is arranged in the inner container, the driving mechanism is in driving connection with the stirrer, and a one-way valve and a water ring vacuum pump are arranged on the pipeline between the receiving tank and the water tank. According to the utility model, the abalone feed liquid is subjected to high-temperature distillation and concentration, so that the steam in the concentration tank can be rapidly pumped to the condenser for condensation and recovery, and the pumping speed of the steam in the concentration tank is higher, thereby improving the concentration efficiency of the abalone feed liquid, and having more evaporation capacity of water and better concentration effect.
Description
Technical Field
The utility model relates to the technical field of vacuum distillation concentration, in particular to a vacuum distillation concentration device for abalone feed liquid.
Background
The abalone peptide is usually extracted and prepared by crushing abalone meat, enzymolysis, enzyme deactivation, filtering and other steps to prepare abalone feed liquid, concentrating, drying and crushing to obtain powdered abalone peptide product.
Disclosure of utility model
The utility model aims to provide a vacuum distillation concentration device for abalone feed liquid, so as to solve the technical problems.
In order to achieve the above purpose, the technical scheme of the utility model is as follows: a vacuum distillation enrichment facility for abalone feed liquid, include concentrated jar, condenser, receiving tank and the water tank of being connected in proper order through the pipeline, concentrated jar is including oily heat preservation, be located oily heat preservation in the inner bag and the sealed lid of demountable installation inner bag top, the electrothermal tube is installed to oily heat preservation's inboard, be provided with the feed inlet on the sealed lid, the bottom of inner bag is provided with control by temperature change probe and discharge gate, the top of sealed lid is provided with actuating mechanism, the inside of inner bag is provided with the agitator, actuating mechanism and agitator drive are connected, install check valve and water ring vacuum pump on the pipeline between receiving tank and the water tank.
Preferably, the condenser is connected above the space between the concentrating tank and the receiving tank, and the viewing cup is arranged on the pipeline between the condenser and the receiving tank.
Preferably, the driving mechanism is a gear motor, the stirrer is a frame stirrer, the frame stirrer comprises a longitudinal main rod, a transverse supporting rod and a U-shaped stirring rod, the transverse supporting rod and the U-shaped stirring rod are arranged at the bottom of the longitudinal main rod, the gear motor is in driving connection with the longitudinal main rod, the middle part of the transverse supporting rod is connected to the longitudinal main rod, and two ends of the transverse supporting rod are connected to the U-shaped stirring rod.
Preferably, the transverse struts are two parallel to each other and respectively perpendicular to the longitudinal main bars.
Preferably, the upper part both sides of the oil heat insulation layer are respectively provided with a liquid inlet and an air outlet, and the lower part both sides are respectively provided with a cold water inlet and a cold water outlet.
Preferably, an interlayer is arranged between the oil thermal insulation layer and the concentration tank.
Preferably, a quick-opening manhole, a vacuum gauge, a cleaning port, a dripping port, an air inlet and two sight glass are arranged on the sealing cover, and a dripping hopper is arranged on the dripping port.
Preferably, the top of the receiving tank is provided with an evacuation port and a vacuum port.
Preferably, the bottoms of the concentrating tank and the receiving tank are respectively provided with a supporting foot stand.
Preferably, the device also comprises a control box, wherein a control circuit board, and a power supply main switch, a temperature controller, a temperature sensor, a stirring switch, an electric heating switch and a vacuum pump switch which are electrically connected with the control circuit board are arranged on the control box.
The utility model has the following beneficial effects:
The utility model comprises a concentrating tank, a condenser, a receiving tank and a water tank which are sequentially connected through a pipeline, wherein the concentrating tank comprises an oil heat insulation layer, an inner container positioned in the oil heat insulation layer and a sealing cover detachably arranged above the inner container, an electric heating pipe is arranged on the inner side of the oil heat insulation layer, a feed inlet is arranged on the sealing cover, a temperature control probe and a discharge hole are arranged at the bottom of the inner container, a driving mechanism is arranged at the top of the sealing cover, a stirrer is arranged in the inner container, the driving mechanism is in driving connection with the stirrer, and a one-way valve and a water ring vacuum pump are arranged on the pipeline between the receiving tank and the water tank. Through the fluid in the electrothermal tube heating oil heat preservation, actuating mechanism drive agitator rotates the stirring to the abalone feed liquid to carry out high temperature distillation concentration to the abalone feed liquid, fluid heating temperature is higher, and be vacuum close-contact intercommunication between concentrated jar, condenser, receiving tank, the water tank, through opening the water ring vacuum pump, make the interior steam of concentrated jar can extract the condenser fast and condense simultaneously, the comdenstion water is finally retrieved through receiving tank, the water tank for the pumping speed of the interior steam of concentrated jar is faster, thereby improves the concentrating efficiency of abalone feed liquid, and the evaporation capacity of moisture is more, and concentrated effect is better.
Drawings
FIG. 1 is a schematic diagram of an embodiment of the present utility model;
fig. 2 is a top view of an embodiment of the present utility model.
Fig. 3 is a schematic structural view of a stirrer according to an embodiment of the present utility model.
The drawings are marked: the device comprises a condenser 1, a receiving tank 2, a water tank 3, a water ring vacuum pump 4, a concentrating tank 5, an oil heat insulating layer 51, a liner 52, a sealing cover 53, a supporting foot rest 6, an electric heating tube 7, a feeding hole 8, a temperature control probe 9, a discharging hole 10, a driving mechanism 11, a stirrer 12, a longitudinal main rod 121, a transverse supporting rod 122, a U-shaped stirring rod 123, a one-way valve 13, a visual cup 14, a liquid inlet 15, a liquid outlet 16, a cold water inlet 17, a liquid outlet 18, an interlayer 19, a quick-opening manhole 20, a vacuum gauge 21, a cleaning hole 22, a dropping hole 23, a gas inlet 24, a viewing mirror 25, a dropping hopper 26, a draining hole 27 and a vacuum hole 28.
Detailed Description
For further illustration of the various embodiments, the utility model is provided with the accompanying drawings. The accompanying drawings, which are incorporated in and constitute a part of this disclosure, illustrate embodiments and together with the description, serve to explain the principles of the embodiments. With reference to these matters, one of ordinary skill in the art will understand other possible embodiments and advantages of the present utility model. The components in the figures are not drawn to scale and like reference numerals are generally used to designate like components.
Referring to fig. 1-3, as an embodiment of the present utility model, there is provided a vacuum distillation concentration device for abalone feed liquid, comprising a concentration tank 5, a condenser 1, a receiving tank 2 and a water tank 3 sequentially connected by a pipeline, wherein the bottoms of the concentration tank 5 and the receiving tank 2 are respectively provided with a support foot stand 6, thereby forming a stable support, the concentration tank 5 comprises an oil thermal insulation layer 51, an inner container 52 positioned in the oil thermal insulation layer 51 and a sealing cover 53 detachably arranged above the inner container 52, an electric heating tube 7 is arranged at the inner side of the oil thermal insulation layer 51, a feed inlet 8 is arranged on the sealing cover 53, a temperature control probe 9 and a discharge outlet 10 are arranged at the bottom of the inner container 52, a driving mechanism 11 is arranged at the top of the sealing cover 53, a stirrer 12 is arranged in the inner container 52, the driving mechanism 11 is in driving connection with the stirrer 12, and a one-way valve 13 and a water ring vacuum pump 4 are arranged on the pipeline between the receiving tank 2 and the water tank 3.
Above-mentioned technical scheme, through throwing into the concentrate jar 5 with the abalone feed liquid through feed inlet 8 in, the fluid in the oily heat preservation 51 of electrothermal tube 7 heating, actuating mechanism 11 drive agitator 12 rotates and stirs the abalone feed liquid, thereby carry out high temperature distillation concentration to the abalone feed liquid, fluid heating temperature is higher, and concentrate jar 5, condenser 1, receiving tank 2, be vacuum close-contact intercommunication between the water tank 3, through opening water ring vacuum pump 4, make the steam in the concentrate jar 5 can be extracted fast and condensate 1, the comdenstion water is finally retrieved through receiving tank 2, water tank 3, this setting makes the pumping speed of the steam in the concentrate jar 5 faster, thereby improve the concentrating efficiency of abalone feed liquid, the evaporation capacity of moisture is more, the concentrating effect is better.
In this embodiment, condenser 1 connects the top between concentrated jar 5 and receiving tank 2 to be convenient for carry out the distillation extraction and the vapor recovery of abalone feed liquid, install on the pipeline between condenser 1 and the receiving tank 2 and look at handlely cup 14, thereby the convenience is looked over at any time and is monitored the water in the pipeline and has or not flowing, knows operating condition.
In this embodiment, the driving mechanism 11 is a gear motor, the stirrer 12 is a frame stirrer 12, which comprises a longitudinal main rod 121, a transverse support rod 122 arranged at the bottom of the longitudinal main rod 121, and a U-shaped stirring rod 123, wherein the gear motor is in driving connection with the longitudinal main rod 121, the middle part of the transverse support rod 122 is connected to the longitudinal main rod 121, the two ends of the transverse support rod are connected to the U-shaped stirring rod 123, the transverse support rod 122 is two mutually parallel and is mutually perpendicular to the longitudinal main rod 121 respectively, and the setting makes the stirrer 12 fully stir, overturn and scrape the abalone feed liquid during concentration, so that the concentration of the abalone feed liquid is more uniform, and the concentration efficiency and the concentration quality of the abalone feed liquid are improved.
In this embodiment, two sides of the upper portion of the oil thermal insulation layer 51 are respectively provided with a liquid inlet 15 and an air outlet 16, the liquid inlet 15 is connected with an oil tank for oil liquid input, two sides of the lower portion are respectively provided with a cold water inlet 17 and an air outlet 18 for adjusting the temperature of the oil liquid and discharging the oil liquid.
In this embodiment, an interlayer 19 is disposed between the oil thermal insulation layer 51 and the concentrating tank 5, so as to reduce heat conduction between the two layers, thereby achieving a more ideal thermal insulation effect.
In this embodiment, quick-opening manhole 20, vacuum gauge 21, cleaning port 22, drip opening 23, air inlet 24, two sight glass 25 have been seted up on the sealed lid 53, install the drip hopper 26 that volume is 30L on the drip opening 23 to conveniently add the abalone feed liquid fast, quick-opening manhole 20 makes things convenient for personnel to go into and out the maintenance, and vacuum gauge 21 is used for detecting the pressure and the vacuum level of concentrated jar 5, and cleaning port 22 makes things convenient for external cleaning line, thereby cleans concentrated jar 5 inside, and two sight glass 25 then conveniently observe the concentrated state of concentrated jar 5 inside.
In this embodiment, the top of the receiving tank 2 is provided with an evacuation port 27 and a vacuum port 28, the evacuation port 27 is used for exhausting air in the receiving tank 2, and the vacuum port 28 is used for being in butt joint with a pipeline to be communicated with the water tank 3.
In this embodiment, the device further includes a control box (not shown in the figure), and a control circuit board, a power main switch electrically connected with the control circuit board, a temperature controller, a temperature sensor, a stirring switch, an electric heating switch, and a vacuum pump switch are mounted on the control box, and are respectively used for controlling and driving each component of the device to work.
In this embodiment, the height of the concentrating tank 5 is 900-1300 mm, the diameter is 800mm, the volume of the concentrating tank 5 is 500L, 600kg of abalone feed liquid can be stored, and finally 100kg of abalone slurry is concentrated, the height of the receiving tank 2 is 500-800 mm, and the diameter is 600mm.
While the utility model has been particularly shown and described with reference to a preferred embodiment, it will be understood by those skilled in the art that various changes in form and details may be made therein without departing from the spirit and scope of the utility model as defined by the appended claims.
Claims (10)
1. A vacuum distillation enrichment facility for abalone feed liquid, its characterized in that: including concentrated jar, condenser, receiving tank and the water tank that connect in proper order through the pipeline, concentrated jar includes oily heat preservation, be located oily heat preservation in the inner bag and demountable installation sealed lid of inner bag top, and the electrothermal tube is installed to oily heat preservation's inboard, and sealed covering is provided with the feed inlet, and the bottom of inner bag is provided with control by temperature change probe and discharge gate, and sealed top of lid is provided with actuating mechanism, and the inside of inner bag is provided with the agitator, and actuating mechanism is connected with the agitator drive, installs check valve and water ring vacuum pump on the pipeline between receiving tank and the water tank.
2. A vacuum distillation concentration device for abalone feed according to claim 1 wherein: the condenser is connected above between the concentrating tank and the receiving tank, and a viewing cup is arranged on a pipeline between the condenser and the receiving tank.
3. A vacuum distillation concentration device for abalone feed according to claim 1 wherein: the driving mechanism is a gear motor, the stirrer is a frame stirrer, the stirrer comprises a longitudinal main rod, a transverse supporting rod and a U-shaped stirring rod, the transverse supporting rod and the U-shaped stirring rod are arranged at the bottom of the longitudinal main rod, the gear motor is in driving connection with the longitudinal main rod, the middle part of the transverse supporting rod is connected to the longitudinal main rod, and the two ends of the transverse supporting rod are connected to the U-shaped stirring rod.
4. A vacuum distillation concentration device for abalone feed according to claim 3 wherein: the transverse support rods are two parallel to each other and are respectively perpendicular to the longitudinal main rod.
5. A vacuum distillation concentration device for abalone feed according to claim 1 wherein: the upper part both sides of the oil heat insulating layer are respectively provided with a liquid inlet and an air outlet, and the lower part both sides are respectively provided with a cold water inlet and an air outlet.
6. A vacuum distillation concentration device for abalone feed according to claim 1 wherein: an interlayer is arranged between the oil thermal insulation layer and the concentration tank.
7. A vacuum distillation concentration device for abalone feed according to claim 1 wherein: the sealing cover is provided with a quick-opening manhole, a vacuum gauge, a cleaning port, a dripping port, an air inlet and two sight glass, and the dripping port is provided with a dripping hopper.
8. A vacuum distillation concentration device for abalone feed according to claim 1 wherein: an evacuation port and a vacuum port are formed in the top of the receiving tank.
9. A vacuum distillation concentration device for abalone feed according to claim 1 wherein: the bottoms of the concentrating tank and the receiving tank are respectively provided with a supporting foot rest.
10. A vacuum distillation concentration device for abalone feed according to claim 1 wherein: the device also comprises a control box, wherein a control circuit board, a power supply main switch, a temperature controller, a temperature sensor, a stirring switch, an electric heating switch and a vacuum pump switch are arranged on the control box, and the power supply main switch, the temperature controller, the temperature sensor, the stirring switch, the electric heating switch and the vacuum pump switch are electrically connected with the control circuit board.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322417322.3U CN220801964U (en) | 2023-09-06 | 2023-09-06 | Vacuum distillation concentration device for abalone feed liquid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322417322.3U CN220801964U (en) | 2023-09-06 | 2023-09-06 | Vacuum distillation concentration device for abalone feed liquid |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220801964U true CN220801964U (en) | 2024-04-19 |
Family
ID=90675363
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202322417322.3U Active CN220801964U (en) | 2023-09-06 | 2023-09-06 | Vacuum distillation concentration device for abalone feed liquid |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220801964U (en) |
-
2023
- 2023-09-06 CN CN202322417322.3U patent/CN220801964U/en active Active
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