CN2057310U - High-efficient energy-saving vacuum cooling rotary steamer - Google Patents
High-efficient energy-saving vacuum cooling rotary steamer Download PDFInfo
- Publication number
- CN2057310U CN2057310U CN89218967U CN89218967U CN2057310U CN 2057310 U CN2057310 U CN 2057310U CN 89218967 U CN89218967 U CN 89218967U CN 89218967 U CN89218967 U CN 89218967U CN 2057310 U CN2057310 U CN 2057310U
- Authority
- CN
- China
- Prior art keywords
- vacuum tube
- steamer
- pot body
- pipe
- vacuum
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
Images
Abstract
The utility model discloses a vacuum cooling rotary steamer which belongs to a kind of raw material boiling device for soy sauce brewing industry. A vacuum tube of the utility model is simultaneously acted as a steam admission pipe and a steam exhaustion pipe, and the vacuum tube vertically and upwards extends to the upper space of the materials from the steamer body and sprays into steam from the space. The two ends of the vacuum tube is respectively provided with an external supporting frame and an inner supporting shaft, the end of a hollow shaft is provided with a self-adjusting end sealing device, and the steamer body is provided with a materials suction concave steamer cover. The utility model has the advantages of materials suction by original steamer, quick heating up, pressure rising and pressure releasing and fast cooling and is capable of meeting the requirements of high-short technology, clinker mechanical conveying and case type conveying.
Description
The utility model relate to a kind ofly make soy sauce, industry low pressure class material cooking equipment such as sauce class, wine vinegar.
At present, brewing industry both domestic and external, at the boiling soya-bean cake, generally need in the raw material processes such as wheat bran 120 ℃-127 ℃ of boiling temperatures, cooking pressure boiling under conditions such as 1.5 kilograms-2 kilograms, take off pressure then, and be quickly cooled to 40 ℃-45 ℃, if can not satisfy these conditions on the technology, so, the raw material of boiling is easy to generate protein not sex change or excessively sex change, like this, all can reduce the utilization rate of material protein, and existing boiling soya-bean cake, the vacuum cooled revolution steamer (abbreviation steamer) of raw materials such as wheat bran, when satisfying above-mentioned process conditions, increasing temperature and pressure is slow, take off and press slowly, cooling is slow, thereby energy consumption height, efficient is low, and nitrogen use efficiency does not reach 80% left and right horizontal entirely, and raw material availability is also lower, inquire into its reason, mainly contain following shortcoming:
1. have steamer now, when spraying into the vapour cooking raw material, be to spray into steam to the material bed centre at pot body middle part, and steam inlet pipe mouth of pipe footpath be little by steam inlet pipe, the jetted hole that has on the tube wall is stopped up by the raw material of gelatinization easily, thereby the admission resistance is big, and increasing temperature and pressure is slow.Take off when pressing, evacuation time is also longer.
2. steamer is in operation process, the pot body is around the hollow shaft and the power transmission shaft rotation of its both sides, and the vacuum tube that is sleeved in the hollow shaft is to fix not rotate with the pot body, and pass hollow axle suspension at an end of vacuum tube and be contained in a pot body middle part, and the two ends of vacuum tube all do not have supporting-point, are in quick condition, so be easy to generate radial displacement, can not guarantee the concentricity of vacuum tube and hollow shaft, when steamer turns round, leak serious between vacuum tube and the hollow shaft.Simultaneously, take seriously air cooling but the time, can not reach the vacuum that requires on the technology again, who knows that to making temperature can not rapidly even can't drop to 40 ℃ of inoculation temperatures, cause the power consumption height, efficient is low.
3. in the pot body, two ends all adopt symmetrical convex pot cover up and down, after vacuumizing, during the charging of pot body, need secondary to change lid, insert feed pipe, and like this, both labour intensity was big, was easy to generate leakage again.
The purpose of this utility model, it is shortcoming at existing vacuum cooled revolution steamer, a kind of follow-on vacuum cooled revolution steamer is provided, make it in operation process, minimizing is to material bed resistance when spraying into steam, improve the speed that heats up and boost in the pot body, improve the speed that vacuumizes and be cooled to inoculation temperature, reduce evacuation time, prevent to leak, improve raw material availability, so reach increasing temperature and pressure fast, take off press rapidly, cooling is fast, high efficiency, energy efficient, the purpose that raw material availability is high.
The technical solution of the utility model is as follows: the design is based on existing vacuum cooled revolution steamer, for example the pot body rotates around its both sides hollow shaft and power transmission shaft, pipe-line system such as vacuum tube, water inlet pipe is fixed, it does not rotate together with the pot body, be set with vacuum tube in the hollow shaft, vacuum tube is suit steam inlet pipe and water inlet pipe again.Take following technological improvement measure on this basis again:
1 〉. remove former steam inlet pipe, the sectional area of vacuum tube is increased, make vacuum tube double as steam inlet pipe, blast pipe, the position of vacuum tube one end in the pot body, promptly the middle part of pot body 9 extends to the space of material bed top vertically upward, and the spray vapour mouth of pipe of bleeding just is located at the vacuum tube top of this material bed superjacent air space.Like this, high steam sprays into a pot body by the admission mouth of pipe by vacuum tube sheaf space from the material, like this, has just reduced by the raw material of gelatinization and has stopped up, thereby improved the speed that heats up, boosts in the pot body, has reduced admission and exhaust resistance.
2 〉. vacuum tube one end in the pot body, an internal support axle with the concentricity line of vacuum tube is housed, the internal support axle is with after sliding bearing cooperates, and integral installation is in the internal support axle bed of transmission axle head.The vacuum tube other end in the external side of pot is equipped with the external support frame.The concentricity that this has just guaranteed vacuum tube and hollow shaft has solved hollow shaft and the vacuum tube excessive problem of concentricity when mounted, has improved installation accuracy, has reduced the serious leakage between on-stream vacuum tube of steamer and the hollow shaft.Equally, when vacuum cooled,, accelerated cooling velocity, who knows that to making temperature can be reduced to 40 ℃ of inoculation temperatures rapidly, reduced energy consumption, improved efficient because the axle envelope is not leaked.
3〉take to take off stage by stage pressure, water, gas, material separating opening have been installed at exhaust pipe mouth.This not only makes and takes off the shortening of pressure time, and pressure is taken off in exhaust fast, and does not run material, has solved existing steamer and has taken off fast when pressing, and the material spray phenomenon of generation has also reduced environmental pollution simultaneously.
4〉at the outer filler bag gland position of the external side of pot, between vacuum tube and the hollow shaft, installed the self-regulated face seals additional, thereby further reduced leakage.
5〉on the pot body of the symmetric position of pot cover, an original convex pot cover is adapted as a suction spill pot cover, snap joint and ball valve have been installed on the spill pot cover, be shaped on material sucking port in the snap joint, both kept the symmetry of pot body, need when having reduced original suction again change lid twice, improved efficient, reduce leak condition, alleviated labour intensity, operation has also made things convenient for.
The utility model is described in further detail below in conjunction with description of drawings and embodiment:
Fig. 1 is a high-efficiency energy-saving vacuum cooling revolution steamer structural representation
Fig. 2 is a hollow shaft sealing device schematic diagram (I)
Fig. 3 is inner supporting structure schematic diagram (II)
Fig. 4 is a suction spill cover structure schematic diagram (III)
Fig. 5 is a self-regulated face seals schematic diagram
Fig. 6 is existing vacuum cooled gyroaxis steamer schematic diagram
The 1-water inlet pipe, 2-hollow shaft sealing device, 3-convex pot cover, the 4-spray vapour mouth of pipe of bleeding, 5-inner supporting device, 6-transmission mechanism, the 7-bearing block, 8-suction spill pot cover, 9-pot body, 10-external support frame, 11-exhaust pipe mouth, 12-vacuum tube, the 13-admission mouth of pipe, 14-internal support axle, 15-self-regulated end face seal, the 16-gland, the outer filler bag of 17-, the hollow axle bed of 18-, the 19-hollow shaft, 20-seal cover, 22-internal support axle bed, the 23-power transmission shaft, 24-snap joint, 25-material sucking port, the 26-ball valve, 27-throw-out collar, 28-o shape sealing ring, the 29-rotating ring, the 30-stationary ring, 31-rotating seat, 32-alignment pin, the 33-spring, the 34-spring base.
As shown in the figure, the utility model is an example with 3.5 cubic metres and 5 cubic metres of vacuum cooled revolution steamers, on the basis of original pot of body 9, has removed former steam inlet pipe, the sectional area of vacuum tube 12 is increased 14 square centimeters, make vacuum tube double as steam inlet pipe, gland steam exhauster.After vacuum tube 12 welds with internal support axle 14, whole car system.During installation, internal support axle 14 is with after sliding bearing cooperates, and integral installation is in internal support axle bed 22.The other end of vacuum tube 12 is installed on the external support frame 10 in pot body 9 outsides.To guarantee the two concentricity precision of vacuum tube 12 and internal support axle 14.Medium position in pot body 9, one end of vacuum tube 12 is extended to material bed superjacent air space vertically upward, the spray vapour mouth of pipe 4 of bleeding just is located at the top of this this vacuum tube 12 of material bed superjacent air space, high steam enters from the admission mouth of pipe 13, sprays in pot body 9 from the spray vapour mouth of pipe 4 of bleeding by vacuum tube 12.
Be set with water inlet pipe 1 in vacuum tube 12, during water inlet, water enters in pot body 9 from water inlet pipe mouth, and material (as soya-bean cake, wheat bran etc.) is wetting.The water spray mouth of pipe is approaching with the spray vapour mouth of pipe 4 positions of drawing gas, but spaced-apart.
Outer filler bag 17 in pot body 9 outsides, gland 16 positions, between vacuum tube 12 and the hollow shaft 19, on original sealing device basis, installed self-regulated end face seal 15 additional, self-regulated end face seal 15 is to be assembled by stationary ring 30, rotating ring 29, rotating seat 31, spring 33, spring base 34, alignment pin 32, throw-out collar 27, o shape sealing ring 28.Thereby further strengthened sealing effectiveness, reduced leakage.
On the pot body 9 of the symmetric position of convex pot cover 3, be adapted as a suction spill pot cover 8, on suction spill pot cover 8, snap joint 24 and ball valve 26 have been installed also, be shaped on material sucking port 25 in the snap joint, raw material sucks in the pot bodies 9 from material sucking port 25.So both kept the symmetry of pot body, the operation that need change lid twice when having reduced suction has again alleviated labour intensity, has improved efficient.
On exhaust pipe mouth 11, water, gas, material separating opening have been installed, make steamer when taking off pressure stage by stage, take off pressure fast, and do not run material.
Other structure of present embodiment such as transmission mechanism, all can adopt existing equipment. Advantage of the present utility model:
1. it is fast to heat up, boost. Because spray vapour exhaust tube of the present utility model is located at material layer superjacent air space, is not stopped up by the gelatinization raw material, add that sealing property is good, so the admission resistance is little, heat up, the rate of rise is fast, shortened the time of material boiling, as under 4 kilograms of conditions of identical pipe pressure, the steaming time of giving of original steamer will be changed 25-30 minute, the utility model only needs 10-15 minute, if pressed temperature reaches 120 ℃-127 ℃, when cooking pressure was 1.5 kilograms-2 kilograms, originally will change 24-30 minute pressing time, the utility model only needs 10-12 minute, and efficient improves greatly.
2. take off and press soon, cooling velocity is fast, because gas extraction system resistance of the present utility model is little, adds that the subregion takes off pressure stage by stage, presses soon so take off, as takes off the pressure time and reduces to 1-2 minute in the fastest 5 minutes both at home and abroad by original. Because sealing property of the present utility model is good, vacuum is taken out when cold again, leaks fewly, so take off when cooling off after the pressure, cooling velocity is accelerated. As under same volume pot body, identical match power condition, by 120 ℃-127 ℃ times that are cooled to 45 ℃ of inoculation temperatures of kettle temperature, former steamer needs 40-50 minute, and the utility model only needs 15-18 minute. So energy-conservation and efficient obviously is surprising.
3. good in economic efficiency. Because the utility model good sealing effect, leak few, thereby the suction of former pot, heat up, boost, take off pressures, time of cooling off shortens greatly, and basically can adapt to the desired corresponding conditions of method for high temprature and short time technology that Present Domestic is promoted use outward, improved and who knows digestibility and raw material utilization rate, saved energy consumption, with original steamer contrast, but energy efficient is over half. Also being that grog is mechanical, the process conditions that provide equipment to adapt to box conveying are provided, so the utility model is good technology, good equipment that equipment for making sauce wet goods industry is worth generally popularization.
4. easy for installation, simple to operate. Because vacuum tube adopts inside and outside supporting-point, and vacuum tube is whole car system with the internal support axle, this has just guaranteed the concentricity of hollow shaft and vacuum tube, thereby further guaranteed the precision of hollow shaft and power transmission shaft concentricity, so install easy to adjust, maintenance levelling is also convenient, has prolonged steamer service life. Adopt owing to the utility model again With suction spill pot cover, so when charging, the material sucking port that only needs feed pipe to be screwed in snap joint gets final product, thus simple to operate, alleviated labour intensity.
Claims (3)
1, a kind ofly make soy sauce, industries such as sauce class, wine vinegar are used, include pot body 9, pot cover 3, hollow shaft 19, power transmission shaft 23, vacuum tube 12, water inlet pipe 1, the admission mouth of pipe 13, exhaust pipe mouth 11, steam jet pipe mouth 4, transmission mechanism 6, bearing block 7, vacuum cooled revolution steamer, on the pot body 9 of hollow shaft 19 and power transmission shaft 23 rotations, be set with vacuum tube 12 in the hollow shaft 19, be set with water inlet pipe in the vacuum tube 12, vacuum tube 12 is fixed, it does not rotate with pot body 9, it is characterized in that:
A. this steamer is by vacuum tube 12 double as steam inlet pipes, blast pipe, in pot body 9, the position of vacuum tube 12 1 ends extends to the space of material bed top vertically upward by the middle part of pot body 9, and the spray vapour mouth of pipe 4 of bleeding just is located at the top of the vacuum tube 12 of this material bed superjacent air space.
B. an end of the vacuum tube in pot body 9 12 is equipped with the internal support axle 14 with vacuum tube 12 concentricity lines, and internal support axle 14 is installed in the internal support axle bed 22 with after sliding bearing cooperates, and at the other end of the vacuum tube 12 in pot body 9 outsides external support frame 10 is housed.
2, vacuum cooled revolution steamer according to claim 1 is characterized in that vacuum tube 12 is sleeved in the hollow shaft 19, and self-regulated face seals 15 has also been adopted in sealing between vacuum tube 12 and the hollow shaft 19.Self-regulated face seals 15 is made up of stationary ring 30, rotating ring 29, rotating seat 31, spring 33, spring base 34, alignment pin 32, throw-out collar 27, o shape sealing ring 28.
3, according to the described vacuum cooled revolution of claim 1 steamer, it is characterized in that on the pot body 9 of pot cover 3 symmetric positions, a suction spill pot cover 8 being housed, the snap joint 24 and the ball valve 26 that are shaped on material sucking port 25 also have been installed on the spill pot cover 8.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN89218967U CN2057310U (en) | 1989-11-03 | 1989-11-03 | High-efficient energy-saving vacuum cooling rotary steamer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN89218967U CN2057310U (en) | 1989-11-03 | 1989-11-03 | High-efficient energy-saving vacuum cooling rotary steamer |
Publications (1)
Publication Number | Publication Date |
---|---|
CN2057310U true CN2057310U (en) | 1990-05-23 |
Family
ID=4873930
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN89218967U Withdrawn CN2057310U (en) | 1989-11-03 | 1989-11-03 | High-efficient energy-saving vacuum cooling rotary steamer |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN2057310U (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104367178A (en) * | 2014-12-12 | 2015-02-25 | 广西大学 | Automatic turning and stirring electric cooker |
CN104814367A (en) * | 2015-05-13 | 2015-08-05 | 宁波长荣酿造设备有限公司 | Pressure relief device for fermentation, and continuous cooking machine using pressure relief device |
CN110373295A (en) * | 2019-08-27 | 2019-10-25 | 湖南博雅智能装备股份有限公司 | Wine brewing steamer |
CN111838545A (en) * | 2020-07-14 | 2020-10-30 | 浙江五芳斋实业股份有限公司 | Processing technology of fresh-keeping rice dumplings |
CN116810383A (en) * | 2023-06-12 | 2023-09-29 | 浙江森车瑞日用品有限公司 | Pot manufacturing equipment and manufacturing method |
-
1989
- 1989-11-03 CN CN89218967U patent/CN2057310U/en not_active Withdrawn
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104367178A (en) * | 2014-12-12 | 2015-02-25 | 广西大学 | Automatic turning and stirring electric cooker |
CN104814367A (en) * | 2015-05-13 | 2015-08-05 | 宁波长荣酿造设备有限公司 | Pressure relief device for fermentation, and continuous cooking machine using pressure relief device |
CN110373295A (en) * | 2019-08-27 | 2019-10-25 | 湖南博雅智能装备股份有限公司 | Wine brewing steamer |
CN111838545A (en) * | 2020-07-14 | 2020-10-30 | 浙江五芳斋实业股份有限公司 | Processing technology of fresh-keeping rice dumplings |
CN116810383A (en) * | 2023-06-12 | 2023-09-29 | 浙江森车瑞日用品有限公司 | Pot manufacturing equipment and manufacturing method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN213090510U (en) | Horizontal condenser | |
CN2057310U (en) | High-efficient energy-saving vacuum cooling rotary steamer | |
CN208587592U (en) | The sealing device of RTO furnace exhaust switching valve | |
CN2432216Y (en) | High-efficiency distillation equipment for making liquor | |
CN210341034U (en) | Nitriding furnace for heat treatment production of corrugated shaft | |
CN208553753U (en) | Compressed air purification system reactor | |
CN110779346A (en) | Steam box tail gas heat recovery system | |
CN213238355U (en) | Packing circulation refrigerating device of drier | |
CN209041118U (en) | A kind of novel saving and the vacuum pump for automatically controlling water ring temperature | |
CN209989247U (en) | Vacuum glass plane sealing device | |
CN212560723U (en) | High-temperature high-pressure dyeing machine with X-shaped reversing structure | |
CN209570016U (en) | A kind of Environmental-protection energy-saving electric liquid furnace | |
CN2406202Y (en) | Normal-pressure high-temp. energy-saving drying barrel | |
CN207091721U (en) | A kind of filter bag production definition device | |
CN206730544U (en) | A kind of vacuum heat-preserving graphite destilling tower | |
CN86205576U (en) | Self-seal extensimeter with multistage, flashing and subtract pressure | |
CN213335615U (en) | Novel energy-concerving and environment-protective heating equipment | |
CN220541440U (en) | Air-cooled heat recovery water chilling unit | |
CN211794155U (en) | Tunnel type steam box inlet and outlet steam self-circulation and exhaust steam recycling system | |
CN212017331U (en) | Energy-saving structure of zero-gas-consumption blast hot dryer | |
CN214821073U (en) | Heat conduction oil circulation heating device used at external temperature | |
CN215114124U (en) | Low-pressure steam utilization device | |
CN216191187U (en) | Cyclohexanone rectification waste liquid recovery device | |
CN209414239U (en) | A kind of late-model inline pump | |
CN220224765U (en) | Steam conveying device for papermaking drying part |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C15 | Extension of patent right duration from 15 to 20 years for appl. with date before 31.12.1992 and still valid on 11.12.2001 (patent law change 1993) | ||
RN01 | Renewal of patent term | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |