CN220276321U - Soybean oligosaccharide vacuum distillation extraction equipment - Google Patents
Soybean oligosaccharide vacuum distillation extraction equipment Download PDFInfo
- Publication number
- CN220276321U CN220276321U CN202321005555.6U CN202321005555U CN220276321U CN 220276321 U CN220276321 U CN 220276321U CN 202321005555 U CN202321005555 U CN 202321005555U CN 220276321 U CN220276321 U CN 220276321U
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- Prior art keywords
- heating
- soybean oligosaccharide
- jar
- heating tank
- heating jar
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- 229920001542 oligosaccharide Polymers 0.000 title claims abstract description 37
- 150000002482 oligosaccharides Chemical class 0.000 title claims abstract description 37
- 235000010469 Glycine max Nutrition 0.000 title claims abstract description 31
- 244000068988 Glycine max Species 0.000 title claims abstract description 30
- 238000000605 extraction Methods 0.000 title claims abstract description 13
- 238000005292 vacuum distillation Methods 0.000 title claims description 6
- 238000010438 heat treatment Methods 0.000 claims abstract description 63
- 238000003756 stirring Methods 0.000 claims abstract description 14
- 238000004821 distillation Methods 0.000 claims abstract description 6
- 238000002156 mixing Methods 0.000 claims abstract description 5
- 239000007788 liquid Substances 0.000 claims description 7
- 238000011068 loading method Methods 0.000 claims description 4
- 230000029058 respiratory gaseous exchange Effects 0.000 claims description 2
- 239000007864 aqueous solution Substances 0.000 abstract description 13
- 238000009835 boiling Methods 0.000 abstract description 3
- 230000002349 favourable effect Effects 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 239000007789 gas Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 235000013527 bean curd Nutrition 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000006837 decompression Effects 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 150000002772 monosaccharides Chemical class 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 235000000346 sugar Nutrition 0.000 description 2
- 229930091371 Fructose Natural products 0.000 description 1
- RFSUNEUAIZKAJO-ARQDHWQXSA-N Fructose Chemical compound OC[C@H]1O[C@](O)(CO)[C@@H](O)[C@@H]1O RFSUNEUAIZKAJO-ARQDHWQXSA-N 0.000 description 1
- 239000005715 Fructose Substances 0.000 description 1
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- 108010073771 Soybean Proteins Proteins 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- WQZGKKKJIJFFOK-PHYPRBDBSA-N alpha-D-galactose Chemical compound OC[C@H]1O[C@H](O)[C@H](O)[C@@H](O)[C@H]1O WQZGKKKJIJFFOK-PHYPRBDBSA-N 0.000 description 1
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 1
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 description 1
- 230000008827 biological function Effects 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 150000002016 disaccharides Chemical class 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 229930182830 galactose Natural products 0.000 description 1
- 230000002496 gastric effect Effects 0.000 description 1
- 239000008103 glucose Substances 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 235000013402 health food Nutrition 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 235000019710 soybean protein Nutrition 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 150000008163 sugars Chemical class 0.000 description 1
- 150000004044 tetrasaccharides Chemical class 0.000 description 1
- 150000004043 trisaccharides Chemical class 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Abstract
The utility model discloses a soybean oligosaccharide reduced pressure distillation extraction device, which comprises a heating tank, wherein two sides of the top surface of the outer side of the heating tank are respectively provided with an electric heater inserted into the heating tank, the middle position of the top surface of the outer side of the heating tank is provided with a driving motor, and the middle position of the top surface of the inner side of the heating tank is provided with a positioning sleeve which is integrated with the tank body of the heating tank; the air inside the heating jar is discharged through the aspirator pump for the heating jar is inside to be in the low pressure environment, reduces soybean oligosaccharide aqueous solution's boiling point, and simultaneously in the heating process, driving motor drives the (mixing) shaft and stirs soybean oligosaccharide aqueous solution, is favorable to soybean oligosaccharide aqueous solution's quick concentration, and this device heats soybean oligosaccharide aqueous solution through electric heater when using, and electric heater adopts the mode of pegging graft to go deep into the inside of heating jar from the top of heating jar, and electric heater's mounting means is simple, easily dismantles, conveniently maintains the change.
Description
Technical Field
The utility model relates to the technical field of soybean oligosaccharide extraction equipment, in particular to soybean oligosaccharide reduced pressure distillation extraction equipment.
Background
The oligosaccharide (or oligosaccharide) is a general term for saccharides whose molecular structure is formed by connecting 2 to 10 monosaccharide molecules with glycosidic bonds. The molecular weight is 300-2000, and the molecular weight is between monosaccharide (glucose, fructose and galactose) and polysaccharide (fiber and starch), and the molecular weight also comprises disaccharide, trisaccharide and tetrasaccharide. The oligosaccharides used as the "specific health food" are oligosaccharides having a specific biological function and being particularly beneficial to gastrointestinal health, and are also called "functional oligosaccharides". Soy oligosaccharides are a generic term for soluble sugars in soybeans.
The bean curd yellow serofluid is rich in soybean protein, oligosaccharide, pigments, salts and the like, wherein the oligosaccharide content accounts for 94% of the total sugar, and is about 12.46g/L. However, because the utilization of yellow serofluid has the problems of large investment, low product yield and the like, the yellow serofluid is discharged as industrial waste liquid, the rich nutrient substances are not utilized, the COD and BOD values are higher, the total nitrogen and ammonia nitrogen are also higher, the yellow serofluid belongs to high-concentration waste water, is extremely perishable and severely pollutes the environment. When soybean oligosaccharide is extracted by using bean curd yellow serofluid as a raw material, the obtained soybean oligosaccharide aqueous solution needs to be heated to concentrate the solution.
Disclosure of Invention
The utility model aims to provide a soybean oligosaccharide reduced pressure distillation extraction device, which aims to solve the problems in the prior art.
In order to achieve the above purpose, the present utility model provides the following technical solutions: the utility model provides a soybean oligosaccharide decompression distillation extraction equipment, includes the heating jar, the electric heater of the inside of inserting the heating jar is respectively installed to the outside top surface both sides of heating jar, a driving motor is installed to the outside top surface intermediate position of heating jar, the inboard top surface intermediate position of heating jar is provided with the cover that is integrated with the jar body of heating jar structure as an organic whole, install the (mixing) shaft in the cover, driving motor's output and (mixing) shaft fixed connection, an aspirator pump is installed respectively to the both sides surface at the outside back of heating jar, the air inlet of aspirator pump communicates with the heating jar through the breathing pipe, and an blast pipe is connected to the gas outlet of aspirator pump, the outside openly of heating jar is provided with the communicating loading hopper with the heating jar, sealed lid is installed at the top of loading hopper.
Preferably, the air outlets of the two suction pumps are connected with the same exhaust pipe, an exhaust port is arranged above the middle part of the exhaust pipe, a liquid outlet is arranged below the middle part of the exhaust pipe, and two radiators are respectively sleeved on two sides of the surface of the exhaust pipe.
Preferably, a section of helical blade is fixed on the upper part and the lower part of the surface of the stirring shaft respectively, a supporting frame is sleeved in the middle of the surface of the stirring shaft, and the supporting frame is fixedly connected with the tank body of the heating tank.
Preferably, a discharge valve is arranged at the discharge hole of the heating tank.
Preferably, support legs are fixedly arranged on two sides of the lower part of the outer side of the heating tank.
Compared with the prior art, the utility model has the beneficial effects that: the air in the heating tank is discharged through the suction pump, so that the heating tank is in a low-pressure environment, the boiling point of the soybean oligosaccharide aqueous solution is reduced, meanwhile, in the heating process, the driving motor drives the stirring shaft to stir the soybean oligosaccharide aqueous solution, the soybean oligosaccharide aqueous solution is favorably concentrated rapidly, the soybean oligosaccharide aqueous solution is heated through the electric heater when the soybean oligosaccharide heating device is used, the electric heater is inserted into the heating tank from the top of the heating tank, and the electric heater is simple in installation mode, easy to detach and convenient to maintain and replace;
the air outlets of the two suction pumps are connected with the same exhaust pipe, the two sides of the exhaust pipe are respectively sleeved with a radiator, the middle of the exhaust pipe is provided with an exhaust port and a liquid outlet, hot and humid air flowing through the exhaust pipe is cooled through the radiator, so that water vapor is condensed into water drops to fall, water-air separation is realized, the hot and humid air is prevented from being directly discharged into the air, the air humidity of the area where the equipment is located is improved, and then the circuit fault of the equipment is caused.
Drawings
The accompanying drawings are included to provide a further understanding of the utility model and are incorporated in and constitute a part of this specification, illustrate the utility model and together with the embodiments of the utility model, serve to explain the utility model. In the drawings:
FIG. 1 is a schematic view of the overall internal structure of the present utility model;
FIG. 2 is a schematic view of the overall rear structure of the present utility model;
fig. 3 is a schematic overall elevational view of the present utility model.
In the figure: 1. a heating tank; 2. an electric heater; 3. a driving motor; 4. a positioning sleeve; 5. a stirring shaft; 6. a support frame; 7. a helical blade; 8. support legs; 9. a discharge valve; 10. an air suction pipe; 11. sealing cover; 12. a hopper; 13. a getter pump; 14. an exhaust pipe; 15. a heat sink; 16. a liquid outlet; 17. and an exhaust port.
Detailed Description
For the purpose of making the objects, technical solutions and advantages of the embodiments of the present utility model more apparent, the technical solutions of the embodiments of the present utility model will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present utility model, and it is apparent that the described embodiments are some embodiments of the present utility model, but not all embodiments. All other embodiments, based on the embodiments of the utility model, which are apparent to those of ordinary skill in the art without inventive faculty, are intended to be within the scope of the utility model. Thus, the following detailed description of the embodiments of the utility model, as presented in the figures, is not intended to limit the scope of the utility model, as claimed, but is merely representative of selected embodiments of the utility model. All other embodiments, based on the embodiments of the utility model, which are apparent to those of ordinary skill in the art without inventive faculty, are intended to be within the scope of the utility model.
Referring to fig. 1-3, in the embodiment of the utility model, a soybean oligosaccharide decompression distillation extraction device comprises a heating tank 1, wherein an electric heater 2 inserted into the heating tank 1 is respectively arranged at two sides of the outer top surface of the heating tank 1, a driving motor 3 is arranged in the middle of the outer top surface of the heating tank 1, a positioning sleeve 4 which is integrally formed with the tank body of the heating tank 1 is arranged in the middle of the inner top surface of the heating tank 1, a stirring shaft 5 is arranged in the positioning sleeve 4, the output end of the driving motor 3 is fixedly connected with the stirring shaft 5, suction pumps 13 are respectively arranged at two side surfaces of the outer back surface of the heating tank 1, an air inlet of each suction pump 13 is communicated with the heating tank 1 through an air suction pipe 10, an air outlet of each suction pump 13 is connected with an air exhaust pipe 14, a charging hopper 12 communicated with the heating tank 1 is arranged at the front surface of the outer side of the heating tank 1, a sealing cover 11 is arranged at the top of each charging hopper 12, a discharging valve 9 is arranged at the position of the discharging outlet of the heating tank 1, and supporting legs 8 are fixedly arranged at two sides of the lower part of the outer side of the heating tank 1.
The air outlets of the two suction pumps 13 are connected with the same exhaust pipe 14, an exhaust port 17 is arranged above the middle part of the exhaust pipe 14, a liquid outlet 16 is arranged below the middle part of the exhaust pipe 14, and two radiators 15 are respectively sleeved on two sides of the surface of the exhaust pipe 14.
The upper part and the lower part of the surface of the stirring shaft 5 are respectively fixed with a section of helical blade 7, a supporting frame 6 is sleeved at the middle position of the surface of the stirring shaft 5, and the supporting frame 6 is fixedly connected with the tank body of the heating tank 1.
The working principle of the utility model is as follows: the air in the heating tank 1 is discharged through the suction pump 13, so that the heating tank 1 is in a low-pressure environment, the boiling point of the soybean oligosaccharide aqueous solution is reduced, meanwhile, in the heating process, the driving motor 3 drives the stirring shaft 5 to stir the soybean oligosaccharide aqueous solution, the soybean oligosaccharide aqueous solution is favorably concentrated rapidly, the soybean oligosaccharide aqueous solution is heated through the electric heater 2 when the soybean oligosaccharide heating device is used, the electric heater 2 is inserted from the top of the heating tank 1 to the inside of the heating tank 1, the electric heater 2 is simple in installation mode and easy to detach, and maintenance and replacement are convenient;
the gas outlets of the two suction pumps 13 are connected with the same exhaust pipe 14, the two sides of the exhaust pipe 14 are respectively sleeved with a radiator 15, the middle part of the exhaust pipe 14 is provided with an exhaust port 17 and a liquid outlet 16, and the hot and humid air flowing through the exhaust pipe 14 is cooled through the radiator 15, so that the water vapor is condensed into water drops to fall down, the water-gas separation is realized, the hot and humid air is prevented from being directly discharged into the air, the air humidity of the area where the equipment is located is improved, and the equipment circuit is further caused.
Finally, it should be noted that: the foregoing description is only a preferred embodiment of the present utility model, and the present utility model is not limited thereto, but it is to be understood that modifications and equivalents of some of the technical features described in the foregoing embodiments may be made by those skilled in the art, although the present utility model has been described in detail with reference to the foregoing embodiments. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present utility model should be included in the protection scope of the present utility model.
Claims (5)
1. The soybean oligosaccharide reduced pressure distillation extraction equipment comprises a heating tank (1), and is characterized in that: the electric heater (2) of the inside of heating jar (1) is respectively installed to outside top surface both sides of heating jar (1), a driving motor (3) is installed to outside top surface intermediate position of heating jar (1), the inboard top surface intermediate position of heating jar (1) is provided with locating sleeve (4) as an organic whole structure with the jar body of heating jar (1), install (mixing) shaft (5) in locating sleeve (4), the output and (mixing) shaft (5) fixed connection of driving motor (3), a suction pump (13) is respectively installed on the both sides surface of the outside back of heating jar (1), the air inlet of suction pump (13) is through breathing pipe (10) and heating jar (1) intercommunication, and blast pipe (14) are connected to the gas outlet of suction pump (13), the outside front of heating jar (1) be provided with the communicating loading hopper (12) of heating jar (1), sealed lid (11) are installed at the top of loading hopper (12).
2. The soybean oligosaccharide vacuum distillation and extraction apparatus according to claim 1, wherein: the air outlets of the two suction pumps (13) are connected with the same exhaust pipe (14), an exhaust port (17) is arranged above the middle of the exhaust pipe (14), a liquid outlet (16) is arranged below the middle of the exhaust pipe (14), and two radiators (15) are respectively sleeved on two sides of the surface of the exhaust pipe (14).
3. The soybean oligosaccharide vacuum distillation and extraction apparatus according to claim 1, wherein: the upper part and the lower part of the surface of the stirring shaft (5) are respectively fixed with a section of helical blade (7), a supporting frame (6) is sleeved at the middle position of the surface of the stirring shaft (5), and the supporting frame (6) is fixedly connected with the tank body of the heating tank (1).
4. The soybean oligosaccharide vacuum distillation and extraction apparatus according to claim 1, wherein: a discharge valve (9) is arranged at the discharge hole of the heating tank (1).
5. The soybean oligosaccharide vacuum distillation and extraction apparatus according to claim 1, wherein: support legs (8) are fixedly arranged on two sides of the lower part of the outer side of the heating tank (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321005555.6U CN220276321U (en) | 2023-04-28 | 2023-04-28 | Soybean oligosaccharide vacuum distillation extraction equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321005555.6U CN220276321U (en) | 2023-04-28 | 2023-04-28 | Soybean oligosaccharide vacuum distillation extraction equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220276321U true CN220276321U (en) | 2024-01-02 |
Family
ID=89341919
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321005555.6U Active CN220276321U (en) | 2023-04-28 | 2023-04-28 | Soybean oligosaccharide vacuum distillation extraction equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220276321U (en) |
-
2023
- 2023-04-28 CN CN202321005555.6U patent/CN220276321U/en active Active
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| GR01 | Patent grant |