CN113293086A - Aromatic vinegar brewing equipment and aromatic vinegar brewing process - Google Patents
Aromatic vinegar brewing equipment and aromatic vinegar brewing process Download PDFInfo
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- CN113293086A CN113293086A CN202110508531.1A CN202110508531A CN113293086A CN 113293086 A CN113293086 A CN 113293086A CN 202110508531 A CN202110508531 A CN 202110508531A CN 113293086 A CN113293086 A CN 113293086A
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- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12J—VINEGAR; PREPARATION OR PURIFICATION THEREOF
- C12J1/00—Vinegar; Preparation or purification thereof
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Abstract
The invention discloses aromatic vinegar brewing equipment and an aromatic vinegar brewing process, and belongs to the technical field of aromatic vinegar brewing equipment. According to the invention, through the mutual matching of the designed structures such as the separation membrane, the pressure relief pipe, the elastic supporting device, the threaded rod, the flow dividing body, the mixed fluid, the flow dividing fan, the mixed flow fan, the booster water pump, the first condensate pipeline and the second condensate pipeline, the membrane separation technology is utilized, the separation efficiency is high, the practicability is strong, the cost is low, the condensation effect on steam can be improved, a certain cooling effect can be realized when low-temperature low-moisture steam is associated with high-temperature high-moisture steam, the water content in the high-temperature high-moisture steam can be reduced, the utilization rate of the condensate can be further improved, the booster water pump can be driven to conduct drainage work when the driving fan blades are subjected to the acting force from the air pressure in the second diversion pipeline, the circulation work of the condensate is realized, and additional driving equipment is not needed.
Description
Technical Field
The invention belongs to the technical field of aromatic vinegar brewing equipment, and particularly relates to aromatic vinegar brewing equipment and an aromatic vinegar brewing process.
Background
The aromatic vinegar has five characteristics of color, fragrance, acidity, mellowness and richness, has clear color, soft sourness, strong vinegar fragrance, pure flavor, mild mouthfeel, fragrance, slight sweetness, dense color and delicious taste, has unchanged quality after long-term storage, and is more aromatic and mellowness.
Prepared by fermentation (wine, vinegar, soy sauce, etc.), ming li shi zhen (compendium of materia Medica, six grass, aconite): "Tu Fu Zi" has everywhere, the root, seedling, flower and fruit are the same as those of Chuan Wu, but it is wild and there is no brewing method, "Zhang Tian Yi" Da Lin and Xiao Lin ": "the purplishment suddenly thinks about a thing: he listens to the fact that the insects can brew a sweet toy, and the insects are very delicious
Cereal need cook when fermenting and making vinegar, can produce a large amount of steam at the in-process of cooking, need condense recycle to steam in order to improve the utilization ratio of heat energy, at present, current condensation equipment for steam still has some weak points in the in-process that uses, and the low-usage of condensate leads to the condensation liquefaction cost higher, and the condensation is inefficient, consequently, the urgent need for a fragrant vinegar makes equipment and method and solves above-mentioned problem on the market at present stage.
Disclosure of Invention
The invention aims to: the device and the method for brewing the aromatic vinegar are provided for solving the problems that the existing condensing device for steam has some defects in the using process, the utilization rate of condensate is low, the condensing and liquefying cost is high, and the condensing efficiency is low.
In order to achieve the purpose, the invention adopts the following technical scheme:
a fragrant vinegar brewing device comprises a condensing tank, wherein a spiral condensing tank is arranged inside the condensing tank, one end of the spiral condensing tank is clamped on one side of a branch fluid close to the condensing tank, one side of the branch fluid deviating from the spiral condensing tank is fixedly connected with a mixed fluid, a mixed fluid fan is arranged in the mixed fluid, the other end of the spiral condensing tank is communicated with one side of a purifying tank close to the purifying tank through a first flow guide pipeline, a separation membrane is arranged in the purifying tank, one end of the purifying tank deviating from the first flow guide pipeline is communicated with one side of a driving box close to the driving box through a second flow guide pipeline, a pressure relief pipe is arranged on the second flow guide pipeline, a driving fan blade is arranged in the driving box, one side of the driving box deviating from the second flow guide pipeline is communicated with one side of the mixed fluid close to the third flow guide pipeline, and the driving fan blade is fixedly connected to the surface of a third rotary shaft, the surface of third switching axle has cup jointed the third bearing, the third bearing joint is on the inside wall of drive box, the tip of third switching axle and the one end fixed connection that booster water pump drive shaft is close, booster water pump's input port is linked together through the one side that first condensate pipeline is close with the condensate piggy bank, the another side of condensate piggy bank is linked together through the one end that second condensate pipeline and condensate tank are close to fluid mixture, the other end of condensate tank is linked together through the delivery outlet of third condensate pipeline and booster water pump.
As a further description of the above technical solution:
the outer periphery of reposition of redundant personnel and the inside wall fixed connection of condensing tank, the reposition of redundant personnel has been seted up the reposition of redundant personnel hole on being close to the one side of mixing the fluid, the reposition of redundant personnel downthehole cover is equipped with the reposition of redundant personnel fan, it is articulated with the inside wall of reposition of redundant personnel hole through the round pin axle on the periphery of reposition of redundant personnel fan.
As a further description of the above technical solution:
the mixed flow fan is fixedly connected to the surface of the first transfer shaft, a first bearing is sleeved on the surface of the first transfer shaft, and the first bearing is clamped on the surface, close to the flow splitting body, of the first bearing.
As a further description of the above technical solution:
the condensation jar corresponds the one end joint of fluid mixture and has the steam contact tube, be provided with first valve on the steam contact tube to the tip of steam contact tube is linked together through first external inlet tube and the close one side of fluid mixture.
As a further description of the above technical solution:
the surface joint of purifying tank has the bleeder line, just the bleeder line is located the separation membrane and is close to one side of first water conservancy diversion pipeline, be provided with the second valve on the bleeder line.
As a further description of the above technical solution:
the pressure relief pipe is internally provided with a bucket body, the internal valve body that is provided with of bucket body, the one side fixed connection elastic supporting device that the valve body deviates from the second water conservancy diversion pipeline, the one end joint that elastic supporting device kept away from the valve body has the fourth bearing, threaded cylinder has been cup jointed in the fourth bearing, threaded cylinder female connection has the threaded rod, the tip fixedly connected with of threaded rod supports the seat.
As a further description of the above technical solution:
the supporting seat is connected to the inner side wall of the elastic supporting device in a sliding mode, one end, far away from the supporting seat, of the threaded cylinder is fixedly connected with a driven bevel gear, the surface of the driven bevel gear is meshed with a driving bevel gear, the driving bevel gear is fixedly connected to the surface of a second transfer shaft, a second bearing is sleeved on the surface of the second transfer shaft, the second bearing is connected to the inner side wall of the pressure relief pipe in a clamping mode, and one end, far away from the driving bevel gear, of the second transfer shaft is fixedly connected with a knob.
As a further description of the above technical solution:
elastic support device is including connecting the urceolus, the inside wall fixed connection of supporting seat and pressure release pipe is passed through to the surface of connecting the urceolus, connect the inside of urceolus and cup jointed the interior pole of connection, the one end of pole is close with the valve body in the connection one end fixed connection, the other end fixedly connected with supporting spring of pole in the connection, the one end that supporting spring deviates from the pole in the connection with support the seat and be correlated with, support seat sliding connection on the inside wall of connecting the urceolus to fourth bearing joint is connecting the inboard port department of urceolus.
As a further description of the above technical solution:
the surface of the condensate storage tank is provided with a measuring cylinder, and the top of the condensate storage tank is provided with a tank cover.
A method for quickly condensing steam for brewing aromatic vinegar comprises the following process flows:
step S1: the first valve is opened, steam enters the mixed flow body through the external leading pipe from the steam leading-out pipe, flows back into the mixed flow body after being condensed by the spiral condensing tank and filtered by the purifying tank, the low-temperature low-moisture steam flowing back into the mixed flow body can drive the mixed flow fan to rotate, and the flow distributing holes and the flow distributing fan are assisted, so that the low-temperature low-moisture steam and the high-temperature high-moisture steam can be uniformly mixed, the flow speed of the high-temperature high-moisture steam in the spiral condensing tank can be slowed down to a certain extent by utilizing the flow disturbing effect, the condensing effect on the steam can be improved by prolonging the condensing time, and the low-temperature low-moisture steam can realize a certain cooling effect in the process of being associated with the high-temperature high-moisture steam, meanwhile, the water content in the high-temperature high-moisture steam can be reduced, and the utilization rate of the condensate can be further improved;
step S2: the second condensate pipeline and the third condensate pipeline are distributed on the condensing tank in a mode that the low-temperature condensate is positioned at the downstream of the condensing tank, the reflux is led out through the upstream of the condensing tank, the condensing effect is good, and the driving fan blades can drive the booster water pump to conduct drainage work when being subjected to the acting force of air pressure in the second flow guide pipeline, so that the circulating work of the condensate is realized;
step S3: the separation membrane has the capacity of separating liquid and gas, so that the separation of the liquid and the gas can be realized in the purification tank after the steam in the spiral condensation tank is condensed, and the filtered steam water in the purification tank can be discharged through the discharge pipe by operating the second valve;
step S4: the knob is stirred, the driving bevel gear can be driven to rotate in the second bearing through the second adapter shaft, the torque force can be transmitted to the threaded cylinder by utilizing the linkage effect between the driving bevel gear and the driven bevel gear, the threaded cylinder can rotate in the fourth bearing, the abutting seat can perform corresponding piston motion in the connecting outer cylinder under the combined action of the torque force and the thread occlusion force, and the abutting seat can control the compression force on the supporting spring in the moving process, namely the hardness of the supporting spring is changed by changing the compression amount of the supporting spring, because the valve body can be subjected to the pushing force from the internal air pressure of the second diversion pipeline, the valve value of the internal air pressure of the second diversion pipeline can be controlled by changing the hardness of the supporting spring, namely the acting force exerted on the valve body by the internal air pressure of the second diversion pipeline is larger than the air pressure value when the elastic force of the supporting spring is applied to the valve body, can realize the effect of automatic pressure release, can effectively control the drive power that the drive flabellum received through the atmospheric pressure threshold value in the control second water conservancy diversion pipeline, consequently, alright realize the circulation speed of regulation and control condensate in the condensate tank, realize higher-quality condensation effect, still can prevent that the inside atmospheric pressure intensity of second water conservancy diversion pipeline is too high.
A vinegar brewing process, wherein a vinegar brewing apparatus as claimed in any one of claims 1 to 8 is used in the vinegar brewing process.
In summary, due to the adoption of the technical scheme, the invention has the beneficial effects that:
1. according to the invention, through the mutual matching of the designed structures such as the separation membrane, the pressure relief pipe, the elastic supporting device, the threaded rod, the flow dividing body, the mixed fluid, the flow dividing fan, the mixed flow fan, the booster water pump, the first condensate pipeline and the second condensate pipeline, the membrane separation technology is utilized, the separation efficiency is high, the practicability is strong, the cost is low, the condensation effect on steam can be improved, a certain cooling effect can be realized when low-temperature low-moisture steam is associated with high-temperature high-moisture steam, the water content in the high-temperature high-moisture steam can be reduced, the utilization rate of the condensate can be further improved, the booster water pump can be driven to conduct drainage work when the driving fan blades are subjected to the acting force from the air pressure in the second diversion pipeline, the circulation work of the condensate is realized, and additional driving equipment is not needed.
2. In the invention, through the designed purification tank, the separation membrane, the discharge pipe and the second valve, the separation membrane has the capacity of separating liquid and gas, so that the separation of the liquid and the gas can be realized in the purification tank after the steam in the spiral condensation tank is condensed, and the filtered steam water in the purification tank can be discharged through the discharge pipe by operating the second valve, the separation efficiency is high, the practicability is strong, and the cost is low by utilizing the membrane separation technology, the separation efficiency is high, the torsion can be transmitted to the threaded cylinder by utilizing the linkage effect between the driving bevel gear and the driven bevel gear by utilizing the designed discharge pipe, the bucket body, the elastic supporting device, the threaded cylinder, the threaded rod, the abutting seat, the driving bevel gear and the driven bevel gear and stirring the knob to drive the driving bevel gear to rotate in the second bearing through the second adapter shaft, so that the threaded cylinder rotates in the fourth bearing, under the combined action of the torque force and the thread occlusion force, the abutting seat can perform corresponding piston motion in the connecting outer cylinder, and the abutting seat can control the compression force of the supporting spring in the moving process, namely the hardness of the supporting spring is changed by changing the compression amount of the supporting spring, because the valve body can receive the pushing force from the air pressure in the second diversion pipeline, the air pressure threshold value in the second diversion pipeline can be controlled by changing the hardness of the supporting spring, namely the air pressure value when the acting force exerted on the valve body by the air pressure in the second diversion pipeline is larger than the elastic force of the supporting spring, the automatic pressure relief effect can be realized, the driving force exerted on the driving fan blades can be effectively controlled by controlling the air pressure threshold value in the second diversion pipeline, therefore, the circulation speed of condensate in the condensation tank can be regulated, and the better condensation effect can be realized, and the air pressure intensity in the second diversion pipeline can be prevented from being too high.
3. In the invention, through the designed flow dividing body, the mixed fluid, the flow dividing fan, the mixed flow fan, the third diversion pipeline and the flow dividing hole, the first valve is opened, the steam enters the mixed fluid through the external leading pipe from the steam leading-out pipe, flows back into the mixed fluid after being condensed by the spiral condensing tank and filtered by the purifying tank, the low-temperature low-moisture steam flowing back into the mixed fluid can drive the mixed flow fan to rotate, and then the flow dividing hole and the flow dividing fan are assisted, so that the low-temperature low-moisture steam and the high-temperature high-moisture steam can be uniformly mixed, the flow velocity of the high-temperature high-moisture steam in the spiral condensing tank can be slowed down to a certain extent by using the turbulence effect, the condensation effect on the steam can be improved by prolonging the condensation time, and the low-temperature low-moisture steam can realize a certain cooling effect in the process of being associated with the high-temperature high-moisture steam, and the water content in the high-temperature high-moisture steam can be reduced at the same time, the utilization rate of the condensate can be further improved.
4. According to the invention, through the designed booster water pump, the first condensate pipeline, the second condensate pipeline, the condensate storage tank, the driving fan blade and the third condensate pipeline, the distribution form of the second condensate pipeline and the third condensate pipeline on the condensate tank is that the low-temperature condensate is positioned at the downstream of the condensate tank, the reflux is led out through the upstream of the condensate tank, the condensation effect is good, and the driving fan blade can drive the booster water pump to conduct drainage work when being subjected to the acting force from the air pressure in the second guide pipeline, so that the circulation work of the condensate is realized.
Drawings
FIG. 1 is a schematic perspective view of a vinegar brewing apparatus and method according to the present invention;
FIG. 2 is a schematic cross-sectional view of a pressure relief pipe in the vinegar brewing apparatus and method according to the present invention;
FIG. 3 is a schematic perspective view of a purification tank of the vinegar brewing apparatus and method according to the present invention;
FIG. 4 is a schematic perspective view of a driving box of the vinegar brewing apparatus and method according to the present invention;
FIG. 5 is an exploded view of the elastic supporting device of the vinegar brewing apparatus and method according to the present invention;
FIG. 6 is an exploded view of the inner structure of the connecting outer cylinder in the vinegar brewing apparatus and method according to the present invention;
FIG. 7 is a schematic diagram of a spiral condensing tank, a split fluid and a fluid mixture in the vinegar brewing apparatus and method according to the present invention;
FIG. 8 is a schematic structural view of a distribution fan in the vinegar brewing apparatus and method according to the present invention;
FIG. 9 is a schematic perspective view of a fluid distribution structure of the vinegar brewing apparatus and method according to the present invention;
FIG. 10 is a schematic perspective view of the fluid mixture in the vinegar brewing apparatus and method according to the present invention.
Illustration of the drawings:
1. a condensing tank; 2. a spiral condensing tank; 3. a flow divider; 4. a shunt hole; 5. a shunt fan; 6. mixing the fluid; 7. a mixed flow fan; 8. a first transfer shaft; 9. a first bearing; 10. a guide pipe is externally connected; 11. a vapor delivery pipe; 12. a first valve; 13. a first diversion conduit; 14. a purification tank; 15. a separation membrane; 16. a pin shaft; 17. a bleeder tube; 18. a second valve; 19. a second diversion conduit; 20. a pressure relief pipe; 21. a bucket-shaped body; 22. a valve body; 23. an elastic support device; 231. connecting the outer cylinder; 232. connecting the inner rod; 233. a support spring; 24. a supporting seat; 25. a fourth bearing; 26. a threaded barrel; 27. a support seat; 28. a driven bevel gear; 29. a drive bevel gear; 30. a second transfer shaft; 31. a second bearing; 32. a knob; 33. a drive cartridge; 34. driving the fan blades; 35. a third transfer shaft; 36. a third bearing; 37. a third diversion conduit; 38. a booster water pump; 39. a first condensate conduit; 40. a condensate reservoir tank; 41. a measuring cylinder; 42. a can lid; 43. a second condensate conduit; 44. a third condensate conduit; 45. a threaded rod.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Referring to fig. 1-10, the present invention provides a technical solution: a fragrant vinegar brewing device comprises a condensing tank 1, a spiral condensing tank 2 is arranged inside the condensing tank 1, one end of the spiral condensing tank 2 is clamped on one side close to a flow distribution body 3, one side of the flow distribution body 3 departing from the spiral condensing tank 2 is fixedly connected with a mixed fluid 6, a mixed flow fan 7 is arranged in the mixed flow body 6, the other end of the spiral condensing tank 2 is communicated with one side close to a purifying tank 14 through a first flow guide pipeline 13, a separation membrane 15 is arranged in the purifying tank 14, one end of the purifying tank 14 departing from the first flow guide pipeline 13 is communicated with one side close to a driving box 33 through a second flow guide pipeline 19, a pressure relief pipe 20 is arranged on the second flow guide pipeline 19, a driving fan blade 34 is arranged in the driving box 33, one side of the driving box 33 departing from the second flow guide pipeline 19 is communicated with one side close to the mixed flow body 6 through a third flow guide pipeline 37, the driving fan blade 34 is fixedly connected to the surface of a third transfer shaft 35, the surface of the third transfer shaft 35 is sleeved with a third bearing 36, the third bearing 36 is clamped on the inner side wall of the driving box 33, the end part of the third transfer shaft 35 is fixedly connected with one end of the third transfer shaft close to the driving shaft of the booster pump 38, the first condensate pipeline 39, the second condensate pipeline 43, the condensate storage tank 40, the driving fan blades 34 and the third condensate pipeline 44 are designed, the distribution form of the second condensate pipeline 43 and the third condensate pipeline 44 on the condensate tank 1 is that low-temperature condensate is positioned at the downstream of the condensate tank 1, backflow is led out through the upstream of the condensate tank 1, the condensation effect is good, the driving fan blades 34 can drive the booster pump 38 to conduct drainage work when being subjected to the acting force from the air pressure in the second diversion pipeline 19, the circulation work of the condensate is realized, the input port of the booster pump 38 is communicated with one side of the condensate storage tank 40 through the first condensate pipeline 39, the other side of the condensate storage tank 40 is communicated with one end of the condensate tank 1 close to the mixed fluid 6 through a second condensate pipeline 43, and the other end of the condensate tank 1 is communicated with an output port of the booster water pump 38 through a third condensate pipeline 44.
Specifically, as shown in fig. 7, the outer circumferential surface of the shunting body 3 is fixedly connected with the inner side wall of the condensing tank 1, one surface of the shunting body 3 close to the mixed fluid 6 is provided with shunting holes 4, shunting fans 5 are sleeved in the shunting holes 4, the circumferential surface of the shunting fan 5 is hinged with the inner side wall of the shunting holes 4 through pin shafts 16, the shunting body 3, the mixed fluid 6, the shunting fan 5, the mixed flow fan 7, a third diversion pipeline 37 and the shunting holes 4 are designed, a first valve 12 is opened, steam enters the mixed flow body 6 through an external guide pipe 10 from a steam guide pipe 11, flows back to the mixed flow body 6 after being condensed by the spiral condensing tank 2 and filtered by the purifying tank 14, the mixed flow fan 7 can be driven to rotate by low-temperature low-moisture steam flowing back into the mixed flow body 6, and then the shunting holes 4 and the shunting fans 5 are assisted, so that the low-temperature low-moisture steam and high-temperature high-moisture steam can be uniformly mixed, utilize the vortex effect, can slow down the flow speed of high temperature high moisture steam in spiral condensing tank 2 to a certain extent, through extension condensation time, can improve the condensation effect to steam, and low temperature low moisture steam can realize certain cooling effect at the in-process that takes place to be correlated with high temperature high moisture steam, still can reduce the water content in the high temperature high moisture steam simultaneously, can further improve the utilization ratio of condensate.
Specifically, as shown in fig. 7, the mixed flow fan 7 is fixedly connected to the surface of the first adapter shaft 8, the first bearing 9 is sleeved on the surface of the first adapter shaft 8, and the first bearing 9 is clamped on the surface close to the splitter 3.
Specifically, as shown in fig. 1, a steam outlet pipe 11 is clamped at one end of the condensation tank 1 corresponding to the mixed fluid 6, a first valve 12 is arranged on the steam outlet pipe 11, and the end of the steam outlet pipe 11 is communicated with one surface of the mixed fluid 6 close to the mixed fluid through a first external connecting pipe 10.
Specifically, as shown in fig. 1, a discharge pipe 17 is clamped on the surface of the purification tank 14, the discharge pipe 17 is located on one side of the separation membrane 15 close to the first diversion pipeline 13, a second valve 18 is arranged on the discharge pipe 17, and through the designed purification tank 14, the separation membrane 15, the discharge pipe 17 and the second valve 18, the separation membrane 15 has the capability of separating liquid and gas, so that the separation of liquid and gas can be realized in the purification tank 14 after the steam in the spiral condensation tank 2 is condensed, and the filtered and intercepted steam water in the purification tank 14 can be discharged through the discharge pipe 17 by operating the second valve 18.
Specifically, as shown in fig. 2, a bucket body 21 is arranged in the pressure relief pipe 20, a valve body 22 is arranged in the bucket body 21, one surface of the valve body 22 away from the second diversion pipeline 19 is fixedly connected with an elastic supporting device 23, one end, far away from the valve body 22, of the elastic supporting device 23 is connected with a fourth bearing 25 in a clamping manner, a threaded cylinder 26 is sleeved in the fourth bearing 25, a threaded rod 45 is connected to the threaded cylinder 26 in an internal thread manner, and the end part of the threaded rod 45 is fixedly connected with a support seat 27.
Specifically, as shown in fig. 1, the abutting seat 27 is slidably connected to an inner side wall of the elastic supporting device 23, one end of the threaded cylinder 26, which is far away from the abutting seat 27, is fixedly connected with a driven bevel gear 28, a driving bevel gear 29 is engaged with a surface of the driven bevel gear 28, the driving bevel gear 29 is fixedly connected to a surface of a second transfer shaft 30, a second bearing 31 is sleeved on a surface of the second transfer shaft 30, the second bearing 31 is clamped on the inner side wall of the pressure relief pipe 20, one end of the second transfer shaft 30, which is far away from the driving bevel gear 29, is fixedly connected with a knob 32, by designing the pressure relief pipe 20, the bucket body 21, the elastic supporting device 23, the threaded cylinder 26, the threaded rod 45, the abutting seat 27, the driving bevel gear 29 and the driven bevel gear 28, the knob 32 is turned, the driving bevel gear 29 is driven to rotate in the second bearing 31 by the second transfer shaft 30, and by utilizing a linkage effect between the driving bevel gear 29 and the driven bevel gear 28, the torque force can be transmitted to the threaded cylinder 26, so that the threaded cylinder 26 rotates in the fourth bearing 25, under the combined action of the torque force and the thread engagement force, the abutting seat 27 can perform corresponding piston motion in the connecting outer cylinder 231, and the abutting seat 27 can control the compression force to the supporting spring 233 in the moving process, that is, the hardness of the supporting spring 233 is changed by changing the compression amount of the supporting spring 233, because the valve body 22 is subjected to the pushing force from the internal air pressure of the second diversion pipeline 19, the internal air pressure of the second diversion pipeline 19 can be controlled by changing the hardness of the supporting spring 233, that is, the acting force exerted by the internal air pressure of the second diversion pipeline 19 on the valve body 22 is greater than the air pressure value when the elastic force of the supporting spring 233, the automatic pressure relief effect can be realized, and the driving force exerted on the driving fan blades 34 can be effectively controlled by controlling the air pressure threshold in the second diversion pipeline 19, therefore, the circulation speed of the condensate in the condensing tank 1 can be regulated and controlled, a better condensing effect can be realized, and the excessive high air pressure intensity in the second diversion pipeline 19 can be prevented.
Specifically, as shown in fig. 2, the elastic supporting device 23 includes a connecting outer cylinder 231, the surface of the connecting outer cylinder 231 is fixedly connected with the inner side wall of the pressure relief pipe 20 through a supporting seat 24, a connecting inner rod 232 is sleeved inside the connecting outer cylinder 231, one end of the connecting inner rod 232 is fixedly connected with the end close to the valve body 22, the other end of the connecting inner rod 232 is fixedly connected with a supporting spring 233, one end of the supporting spring 233 departing from the connecting inner rod 232 is associated with a support seat 27, the support seat 27 is slidably connected on the inner side wall of the connecting outer cylinder 231, and the fourth bearing 25 is clamped at the port of the inner side of the connecting outer cylinder 231.
Specifically, as shown in fig. 8, a measuring cylinder 41 is provided on the surface of the condensate reservoir tank 40, and a cap 42 is provided on the top of the condensate reservoir tank 40.
A method for quickly condensing steam for brewing aromatic vinegar comprises the following process flows:
step S1: the first valve 12 is opened, the steam enters the mixed flow body 6 from the steam outlet pipe 11 through the external leading pipe 10, after being condensed by the spiral condensing tank 2 and filtered by the purifying tank 14, the low-temperature low-moisture steam flows back to the mixed flow body 6, the low-temperature low-moisture steam flowing back to the mixed flow body 6 can drive the mixed flow fan 7 to rotate, and then the mixed flow fan is assisted by the shunt hole 4 and the shunt fan 5, can realize the homogeneous mixing of low-temperature low-moisture steam and high-temperature high-moisture steam, can slow down the flowing speed of the high-temperature high-moisture steam in the spiral condensing tank 2 to a certain extent by utilizing the turbulent flow effect, and can prolong the condensing time, can improve the condensation effect on the steam, and the low-temperature low-moisture steam can realize certain cooling effect in the process of being associated with the high-temperature high-moisture steam, meanwhile, the water content in the high-temperature high-moisture steam can be reduced, and the utilization rate of the condensate can be further improved;
step S2: the second condensate pipeline 43 and the third condensate pipeline 44 are distributed on the condensing tank 1 in a manner that the low-temperature condensate is positioned at the downstream of the condensing tank 1, the reflux is led out through the upstream of the condensing tank 1, the condensing effect is good, and the driving fan blades 34 can drive the booster water pump 38 to conduct drainage work when being subjected to the acting force from the air pressure in the second flow guide pipeline 19, so that the circulating work of the condensate is realized;
step S3: the separation membrane 15 has the capacity of separating liquid and gas, so that the separation of the liquid and the gas can be realized in the purification tank 14 after the steam in the spiral condensation tank 2 is condensed, the filtered and cut-off steam water in the purification tank 14 can be discharged through the discharge pipe 17 by operating the second valve 18, and by utilizing the membrane separation technology, the separation efficiency is high, the practicability is high, and the cost is low;
step S4: the knob 32 is turned, the driving bevel gear 29 is driven by the second transfer shaft 30 to rotate in the second bearing 31, the torque force can be transmitted to the threaded cylinder 26 by utilizing the linkage effect between the driving bevel gear 29 and the driven bevel gear 28, the threaded cylinder 26 rotates in the fourth bearing 25, the abutting seat 27 can perform corresponding piston movement in the connecting outer cylinder 231 under the combined action of the torque force and the thread engagement force, and the abutting seat 27 can control the compression force of the supporting spring 233 in the moving process, namely, the hardness of the supporting spring 233 is changed by changing the compression amount of the supporting spring 233, since the valve body 22 is subjected to the pushing force from the internal air pressure of the second diversion pipeline 19, the internal air pressure of the second diversion pipeline 19 can be controlled by changing the hardness of the supporting spring 233, namely, the acting force of the internal air pressure of the second diversion pipeline 19 on the valve body 22 is larger than the air pressure value when the elastic force of the supporting spring 233 is applied, the effect of automatic pressure release can be realized, the drive power that drive flabellum 34 received can be effectively controlled through the atmospheric pressure threshold in controlling second water conservancy diversion pipeline 19, consequently, alright realize the circulation speed of regulation and control condensate in condensing tank 1, realize better condensation effect, still can prevent that the inside atmospheric pressure intensity of second water conservancy diversion pipeline 19 is too high.
The working principle is as follows: when in use, the separating membrane 15 has the capability of separating liquid and gas, so that the steam in the spiral condensing tank 2 can be separated from the liquid in the purifying tank 14 after being condensed, and the steam water intercepted after being filtered in the purifying tank 14 can be discharged through the discharge pipe 17 by operating the second valve 18, the separating efficiency is high, the practicability is strong, and the cost is low by utilizing the membrane separation technology, the knob 32 is stirred, the driving bevel gear 29 can be driven to rotate in the second bearing 31 through the second transfer shaft 30, the torsion can be transmitted to the threaded cylinder 26 by utilizing the linkage effect between the driving bevel gear 29 and the driven bevel gear 28, the threaded cylinder 26 rotates in the fourth bearing 25, the abutting seat 27 can perform corresponding piston motion 231 in the connecting outer cylinder under the combined action of the torsion and the thread engaging force, and the abutting seat 27 can move 231, the compression force of the supporting spring 233 can be controlled, that is, the hardness of the supporting spring 233 is changed by changing the compression amount of the supporting spring 233, since the valve body 22 is pushed by the air pressure inside the second guiding pipe 19, the valve body can control the air pressure threshold inside the second guiding pipe 19 by changing the hardness of the supporting spring 233, that is, the acting force of the air pressure inside the second guiding pipe 19 on the valve body 22 is larger than the air pressure value when the elastic force of the supporting spring 233 is larger, the automatic pressure relief effect can be realized, the driving force of the driving fan 34 can be effectively controlled by controlling the air pressure threshold inside the second guiding pipe 19, therefore, the circulation speed of the condensate in the condensing tank 1 can be regulated and controlled, the better condensing effect can be realized, the over-high air pressure intensity inside the second guiding pipe 19 can be prevented, the first valve 12 is opened, the steam enters the mixed flow body 6 through the external leading-out pipe 10 from the steam leading-out pipe 11, after being condensed by the spiral condensing tank 2 and filtered by the purifying tank 14, the low-temperature low-moisture steam reflows into the mixed flow body 6 to drive the mixed flow fan 7 to rotate, and then the flow distribution holes 4 and the flow distribution fans 5 are assisted to realize the homogeneous mixing of the low-temperature low-moisture steam and the high-temperature high-moisture steam, the flow speed of the high-temperature high-moisture steam in the spiral condensing tank 2 can be slowed down to a certain extent by utilizing the turbulence effect, the condensing effect on the steam can be improved by prolonging the condensing time, in the process that the low-temperature low-moisture steam is associated with the high-temperature high-moisture steam, a certain cooling effect can be realized, the water content in the high-temperature high-moisture steam can be reduced, the utilization rate of the condensate can be further improved, the distribution form of the second condensate pipeline 43 and the third condensate pipeline 44 on the condensing tank 1 is that the low-temperature condensate is positioned at the downstream of the condensing tank 1, the reflux is led out from the upstream of the condensing tank 1, the condensing effect is good, and the driving fan blades 34 can drive the booster water pump 38 to conduct the drainage work when receiving the acting force from the internal air pressure of the second guide pipeline 19, so that the circulation work of the condensate is realized.
The above description is only for the preferred embodiment of the present invention, but the scope of the present invention is not limited thereto, and any person skilled in the art should be able to cover the technical scope of the present invention and the equivalent alternatives or modifications according to the technical solution and the inventive concept of the present invention within the technical scope of the present invention.
Claims (10)
1. A vinegar brewing device comprises a condensing tank (1) and is characterized in that,
a spiral condensing tank (2) is arranged in the condensing tank (1),
one end of the spiral condensing tank (2) is clamped on one side close to the flow dividing body (3), one side of the flow dividing body (3) deviating from the spiral condensing tank (2) is fixedly connected with a mixed fluid (6), and the mixed fluid isMixed fluid (6)A mixed flow fan (7) is arranged in the inner part,
the other end of the spiral condensing tank (2) is communicated with one surface close to a purifying tank (14) through a first diversion pipeline (13), a separation membrane (15) is arranged in the purifying tank (14),
one end of the purifying tank (14) departing from the first diversion pipeline (13) is communicated with one side of the driving box (33) close to the purifying tank through a second diversion pipeline (19), a pressure relief pipe (20) is arranged on the second diversion pipeline (19), driving fan blades (34) are arranged in the driving box (33), one side of the driving box (33) departing from the second diversion pipeline (19) is communicated with one side of the mixed flow body (6) close to the mixed flow body through a third diversion pipeline (37),
the driving fan blades (34) are fixedly connected to the surface of the third transfer shaft (35), the surface of the third transfer shaft (35) is sleeved with a third bearing (36), the third bearing (36) is clamped on the inner side wall of the driving box (33), the end part of the third transfer shaft (35) is fixedly connected with one end, close to the driving shaft of the booster water pump (38),
the input port of the booster water pump (38) is communicated with one side, close to the condensate storage tank (40), of the condensate storage tank (40) through a first condensate pipeline (39), the other side of the condensate storage tank (40) is communicated with one end, close to the mixed fluid (6), of the condensation tank (1) through a second condensate pipeline (43), and the other end of the condensation tank (1) is communicated with the output port of the booster water pump (38) through a third condensate pipeline (44).
2. A vinegar brewing device according to claim 1, wherein the outer circumferential surface of the shunting body (3) is fixedly connected with the inner side wall of the condensing tank (1), one surface of the shunting body (3) close to the mixing body (6) is provided with shunting holes (4), shunting fans (5) are sleeved in the shunting holes (4), and the circumferential surface of each shunting fan (5) is hinged with the inner side wall of each shunting hole (4) through a pin shaft (16).
3. The vinegar brewing device according to claim 2, wherein the mixed flow fan (7) is fixedly connected to the surface of the first transfer shaft (8), the first bearing (9) is sleeved on the surface of the first transfer shaft (8), the first bearing (9) is clamped on the surface close to the flow dividing body (3), a steam outlet pipe (11) is clamped at one end of the condensation tank (1) corresponding to the mixed fluid (6), a first valve (12) is arranged on the steam outlet pipe (11), and the end of the steam outlet pipe (11) is communicated with the surface close to the mixed flow body (6) through a first external lead pipe (10).
4. A vinegar brewing apparatus according to claim 3, wherein a drain pipe (17) is clamped to the surface of the purification tank (14), and the drain pipe (17) is located at the side of the separation membrane (15) close to the first guide pipe (13), and a second valve (18) is arranged on the drain pipe (17).
5. A vinegar brewing device according to claim 1, wherein a bucket body (21) is arranged in the pressure relief pipe (20), a valve body (22) is arranged in the bucket body (21), an elastic supporting device (23) is fixedly connected to one side of the valve body (22) away from the second flow guide pipeline (19), a fourth bearing (25) is clamped to one end, away from the valve body (22), of the elastic supporting device (23), a threaded cylinder (26) is sleeved in the fourth bearing (25), a threaded rod (45) is connected to the threaded cylinder (26) in an internal thread manner, and an abutting seat (27) is fixedly connected to the end portion of the threaded rod (45).
6. A vinegar brewing device according to claim 5, characterized in that the supporting seat (27) is slidably connected to the inner side wall of the elastic supporting device (23), one end of the threaded cylinder (26) far away from the supporting seat (27) is fixedly connected with a driven bevel gear (28), the surface of the driven bevel gear (28) is meshed with a driving bevel gear (29), the driving bevel gear (29) is fixedly connected to the surface of a second transfer shaft (30), the surface of the second transfer shaft (30) is sleeved with a second bearing (31), the second bearing (31) is clamped on the inner side wall of the pressure relief pipe (20), and one end of the second transfer shaft (30) far away from the driving bevel gear (29) is fixedly connected with a knob (32).
7. The vinegar brewing device according to claim 6, characterized in that the elastic supporting device (23) comprises a connecting outer cylinder (231), the surface of the connecting outer cylinder (231) is fixedly connected with the inner side wall of the pressure relief pipe (20) through a supporting seat (24), a connecting inner rod (232) is sleeved inside the connecting outer cylinder (231), one end of the connecting inner rod (232) is fixedly connected with one end close to the valve body (22), the other end of the connecting inner rod (232) is fixedly connected with a supporting spring (233), one end of the supporting spring (233) departing from the connecting inner rod (232) is associated with a supporting seat (27), the supporting seat (27) is slidably connected on the inner side wall of the connecting outer cylinder (231), and a fourth bearing (25) is clamped at a port on the inner side wall of the connecting outer cylinder (231).
8. A vinegar brewing apparatus according to claim 7, characterized in that the surface of the condensate reservoir (40) is provided with a measuring cylinder (41) and the top of the condensate reservoir (40) is provided with a lid (42).
9. The method for rapidly condensing steam for brewing aromatic vinegar according to the claims 1 to 8, which is characterized by comprising the following process flows:
step S1: the first valve (12) is opened, steam enters the mixed fluid (6) through the external leading pipe (10) from the steam leading-out pipe (11), flows back to the mixed fluid (6) after being condensed by the spiral condensing tank (2) and filtered by the purifying tank (14), low-temperature low-moisture steam flowing back to the mixed fluid (6) can drive the mixed flow fan (7) to rotate, and then is assisted by the shunt hole (4) and the shunt fan (5), so that the low-temperature low-moisture steam and the high-temperature high-moisture steam can be uniformly mixed, the flow speed of the high-temperature high-moisture steam in the spiral condensing tank (2) can be slowed down to a certain extent by utilizing the turbulence effect, the condensing effect on the steam can be improved by prolonging the condensing time, and the low-temperature low-moisture steam can realize a certain cooling effect in the process of being associated with the high-temperature high-moisture steam, and simultaneously the water content in the high-temperature high-moisture steam can be reduced, the utilization rate of the condensate can be further improved;
step S2: the second condensate pipeline (43) and the third condensate pipeline (44) are distributed on the condensing tank (1) in a mode that the low-temperature condensate is positioned at the downstream of the condensing tank (1), the reflux is led out through the upstream of the condensing tank (1), the condensing effect is good, and the driving fan blades (34) are subjected to the condensationFromWhen acting force of air pressure in the second diversion pipeline (19), the booster water pump (38) can be driven to conduct drainage work, and circulation work of condensate is achieved;
step S3: the separation membrane (15) has the capacity of separating liquid and gas, so that the steam in the spiral condensing tank (2) can be separated from the liquid and the gas in the purifying tank (14) after being condensed, the filtered and cut-off steam water in the purifying tank (14) can be discharged through the discharge pipe (17) by operating the second valve (18), and the membrane separation technology is utilized, so that the separation efficiency is high, the practicability is high, and the cost is low;
step S4: the knob (32) is turned, the driving bevel gear (29) is driven to rotate in the second bearing (31) through the second transfer shaft (30), and the torque force can be adjusted by utilizing the linkage effect between the driving bevel gear (29) and the driven bevel gear (28)Conveying appliance Delivery deviceThe threaded cylinder (26) is rotated in the fourth bearing (25), the abutting seat (27) can perform corresponding piston motion in the connecting outer cylinder (231) under the combined action of the torsion force and the thread engagement force, and the abutting seat (27) can control the compression force of the supporting spring (233) in the moving process, namely the hardness of the supporting spring (233) is changed by changing the compression amount of the supporting spring (233), because the valve body (22) is subjected to the pushing force from the internal air pressure of the second diversion pipeline (19), the internal air pressure threshold value of the second diversion pipeline (19) can be controlled by changing the hardness of the supporting spring (233), namely the acting force exerted on the valve body (22) by the internal air pressure of the second diversion pipeline (19) is larger than the air pressure value when the elastic force of the supporting spring (233), and the automatic pressure relief effect can be realized, the driving force applied to the driving fan blades (34) can be effectively controlled by controlling the air pressure threshold value in the second diversion pipeline (19), so that the condensate can be regulated and controlled in the condensing tank(1) The internal circulation speed realizes better condensation effect and can prevent the air pressure intensity inside the second diversion pipeline (19) from being too high.
10. A vinegar brewing process, characterized in that a vinegar brewing apparatus according to any one of the preceding claims 1 to 8 is used in the vinegar brewing process.
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| Application Number | Priority Date | Filing Date | Title |
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| CN202110508531.1A CN113293086A (en) | 2021-05-11 | 2021-05-11 | Aromatic vinegar brewing equipment and aromatic vinegar brewing process |
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| CN202110508531.1A CN113293086A (en) | 2021-05-11 | 2021-05-11 | Aromatic vinegar brewing equipment and aromatic vinegar brewing process |
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| CN113293086A true CN113293086A (en) | 2021-08-24 |
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Cited By (1)
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| CN116242047A (en) * | 2023-05-12 | 2023-06-09 | 泰州库宝制冷设备制造有限公司 | Refrigerating equipment with circulating condensation function and refrigerating method |
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