CN204768688U - Take flow regulator's fermentation reaction cauldron - Google Patents
Take flow regulator's fermentation reaction cauldron Download PDFInfo
- Publication number
- CN204768688U CN204768688U CN201520454353.9U CN201520454353U CN204768688U CN 204768688 U CN204768688 U CN 204768688U CN 201520454353 U CN201520454353 U CN 201520454353U CN 204768688 U CN204768688 U CN 204768688U
- Authority
- CN
- China
- Prior art keywords
- flow regulator
- kettle
- rectifier
- cauldron
- fermentation reaction
- 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.)
- Expired - Fee Related
Links
Landscapes
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
The utility model discloses a take flow regulator's fermentation reaction cauldron, the reactor comprises a kettle, cauldron body top is equipped with inverter motor, a (mixing) shaft that extends to bottom jar body is connected in the inverter motor drive, the bottom and the setting of (mixing) shaft are connected at the fixed cover bottom the cauldron body, set up the stirring stabilizer on the (mixing) shaft, the stirring stabilizer includes the hub, be fixed with cross paddle on the hub, be equipped with cooling coil on the internal wall of cauldron, be equipped with the heating intermediate layer on the external wall of cauldron, cauldron body top is equipped with the feed inlet, the feed inlet is connected with charge -in pipeline and cuts a department in feed inlet upper reaches position, insert flow regulator, flow regulator is including the liquid pump that connects gradually, choke valve and rectifier. The utility model discloses install multilayer cooling coil additional at the internal wall of former intermediate layer cauldron, realized that a cauldron can heat up and refrigerated reaction function the shortening reaction time simultaneously, flow regulator structural design is reasonable, and the installation is dismantled conveniently, easy operation, and safe and reliable is applicable to various reaction environment flow controls.
Description
Technical field
The utility model relates to biology, chemical reactor field, specifically a kind of fermentation reaction still with flow regulator.
Background technology
Still is the rustless steel container of physics or chemical reaction, be widely used in the research of the type of production users such as oil, chemical industry, rubber, agricultural chemicals, dyestuff, medicine, food and various scientific experiment project, be used for the container of the technical process such as hydrolysis, neutralization, crystallization, distillation, evaporation, storage, hydrogenation, hydrocarbonylation, polymerization, condensation, heating mixture, temperature reaction; Traditional reactor many employings interlayer heating, if reaction needed cools, need other equipment, cause many inconvenience for addressing these problems to applying unit, Chinese patent CN203625359U disclose a kind ofly to heat up, the multilayer that cools stirs fermentation reaction tank, enter heat pipe mouth by charging aperture, interlayer, cool cycles water inlet, fixed cover, discharging opening, motor, speed changer, blast pipe, tank body, heating interlayer, multilayer cooling coil, stirring vane, shaft, cool cycles water out, interlayer go out heat pipe mouth, supporting leg forms; This utility model adopts and installs multilayer cooling coil additional at former interlayer inner wall of kettle, achieves the response function that a tank can heat up simultaneously and cool, Reaction time shorten, saves the required energy, have simple and compact for structure, strong and reliable advantage; But in fermentation reaction whipping process, the agitating device of general employing axial-flow type, vibration is produced in order to prevent agitating device, then intermediate bearing will be increased, when using in the reactor that ratio of height to diameter is larger, generally need to increase bottom bearing to support, which adds equipment making and use cost, and, when running up, axial flow type stirrer blade rear can form certain eddy current or air pocket, reduces the stirring efficiency of stirrer paddle, fermentation reaction speed is also had a significant impact, needs improvement badly.
Carrying in the process of various industrial chemicals for reactor simultaneously, the control of flow is vital for chemical reaction, manufacturing enterprise normally completes reaction task according to reactor, after each product or head product preparation, it is detected, or production expectation is detected, judge whether flow exists deviation.In addition, because each equipment especially feed pipe in process of production can be lossy, the flow generation deviation preset can be made, and then impact is produced.
Utility model content
The purpose of this utility model is to provide a kind of fermentation reaction still with flow regulator, to solve the problem proposed in above-mentioned background technology.
For achieving the above object, the utility model provides following technical scheme:
A kind of fermentation reaction still with flow regulator, comprise kettle, kettle top is provided with variable-frequency motor, variable-frequency motor drives the shaft connecting and extend to tank base, the bottom of shaft is connected with the fixed cover being arranged on autoclave body bottom, the shaft being positioned at kettle is evenly distributed with three layers of stirring vane, shaft between adjacent two stirring vanes is arranged one and stir stabilizer, stir stabilizer and comprise wheel hub, wheel hub be circumferentially fixed with cross blade, four blade outer rims of cross blade are arc-shaped and are in circumferentially same, cross blade is fixedly connected with the inwall of stabilizing sleeve, cross blade is located in stabilizing sleeve, stabilizing sleeve is columnar structured, the parallel equal and plane-parallel of upper and lower surface of stabilizing sleeve, chopping disk is provided with in the middle part of the outer rim of stabilizing sleeve, it is annular slab inside chopping disk, outside is for being evenly distributed on the some dentalations in the middle part of annular slab outer rim, the inwall of kettle is provided with multilayer cooling coil, cooling coil is connected with the cool cycles water inlet be arranged on kettle outer wall and cool cycles water out, the outer wall of kettle is provided with heating interlayer, heating interlayer is connected with into heat pipe mouth and goes out heat pipe mouth, charging aperture and blast pipe is provided with at the top of kettle, charging aperture connects right feed pipe, feed pipe blocks a place at charging aperture upstream position, access flow adjusting device, flow regulator comprises the liquid pump connected successively, choke valve and rectifier, a shunt pipe is provided with in rectifier, shunt pipe is provided with electromagnetic flowmeter, electromagnetic flowmeter is fastened on the flow display device of rectifier outside, by arranging the shunt pipe of band electromagnetic flowmeter in rectifier, hand-operated valve wheel is provided with reducing seal cover with the connecting portion of choke valve, hand-operated valve wheel is used for the material flow that manual adjustments enters rectifier, the inside, one end that choke valve is connected with rectifier is also provided with antipriming pipe and sieves, rectifier outer wall is provided with the open-close on-off controlling electromagnetic flowmeter break-make, electromagnetic flowmeter is in closed condition when not working, also screen cloth is installed in feed pipe.
As further program of the utility model: dentalation and annular slab one-body molded, dentalation and annular slab perpendicular, dentalation outer rim mid point is positioned on same circle and this circle place plane is parallel with stabilizing sleeve upper and lower surface, the all faceted portions of dentalation arrange R8 ~ R20 fillet, and dentalation is provided with 6 ~ 8 and is evenly distributed on the circle of annular slab place.
As the utility model further scheme: the top of kettle is provided with charging aperture and blast pipe.
As the utility model further scheme: all connected by flangeseal between feed pipe, liquid pump, choke valve, rectifier.
As the utility model further scheme: described choke valve is provided with hand-operated valve wheel, hand-operated valve wheel, in choke valve symmetric position, respectively installs one.
As the utility model further scheme: the side, bottom of described kettle is also provided with discharging opening.
Compared with prior art, the beneficial effects of the utility model are: the utility model adopts and installs multilayer cooling coil additional at former interlayer inner wall of kettle, achieve the response function that a still can heat up simultaneously and cool, Reaction time shorten, save the required energy, having simple and compact for structure, strong and reliable advantage, is the desirable equipment of fermentation reaction; Stabilizing sleeve in the utility model and chopping disk can limit the swing of the shaft caused by fluid, chopping disk can stop the floating of container bottom input gas on the one hand, reduce ascent rate, increase gas dispersion and soak time, can shred bubble or associated media on the other hand, increase medium response area, accelerate mix and blend speed; Flow regulator reasonable in design in the utility model, the raw material flow rate entering reactor can be regulated, control in real time according to response situation, easy installation and removal, simple to operate, safe and reliable, be applicable to various reaction environment amount and control, avoid the hysteresis quality of velocity of flow adjust, relative inexpensiveness, be easy to detect, clear up and regular maintenance, this segmentation structure is convenient to detect each functional part, clear up and regular maintenance, alleviates the workload of attendant.
Accompanying drawing explanation
Fig. 1 is the structural representation of the fermentation reaction still of band flow regulator;
Fig. 2 is the structural representation of flow regulator in the fermentation reaction still of band flow regulator;
Fig. 3 is the front view stirring stabilizer in the fermentation reaction still of band flow regulator;
Fig. 4 is the top view stirring stabilizer in the fermentation reaction still of band flow regulator;
In figure: 1-variable-frequency motor, 2-charging aperture, 3-blast pipe, 4-kettle, 5-stirs stabilizer, 6-cooling coil, 7-cool cycles water out, 8-goes out heat pipe mouth, 9-discharging opening, 10-fixed cover, 11-shaft, 12-stirring vane, 13-heating interlayer, 14-cool cycles water inlet, 15-enters heat pipe mouth, 16-feed pipe, 17-liquid pump, 18-choke valve, 19-rectifier, 20-shunt pipe, 21-electromagnetic flowmeter, 22-flow display device, 23-hand-operated valve is taken turns, 24-seal cover, 25-ring flange, 26-open-close on-off, 27-antipriming pipe sieves, 28-screen cloth, 51-wheel hub, 52-blade, 53-stabilizing sleeve, 54-gear structure.
Detailed description of the invention
Be described in more detail below in conjunction with the technical scheme of detailed description of the invention to this patent.
Refer to Fig. 1-3, a kind of fermentation reaction still with flow regulator, comprise kettle 4, kettle 4 top is provided with variable-frequency motor 1, variable-frequency motor 1 drives the shaft 11 connecting and extend to tank base, the bottom of shaft 11 is connected with the fixed cover 10 be arranged on bottom kettle 4, the shaft 11 being positioned at kettle 4 is evenly distributed with three layers of stirring vane 12, shaft 11 between adjacent two stirring vanes 12 is arranged one and stir stabilizer 5, stir stabilizer 5 and be made up of wheel hub 51, blade 52, stabilizing sleeve 53 and circle chopping disk; Wheel hub 51 be circumferentially fixed with cross blade 52, four blade outer rims of cross blade 52 are arc-shaped and are in circumferentially same, and cross blade is fixedly connected with the inwall of stabilizing sleeve 53, and cross blade is located in stabilizing sleeve 53; Stabilizing sleeve 53 is columnar structured, the parallel equal and plane-parallel of upper and lower surface of stabilizing sleeve 53; Chopping disk is provided with in the middle part of the outer rim of stabilizing sleeve 53, it is annular slab inside chopping disk, outside is for being evenly distributed on the some dentalations 54 in the middle part of annular slab outer rim, dentalation 54 is one-body molded with annular slab, dentalation 54 and annular slab perpendicular, dentalation 54 outer rim mid point is positioned on same circle and this circle place plane is parallel with stabilizing sleeve 53 upper and lower surface, the all faceted portions of dentalation 54 arrange R8 ~ R20 fillet, and dentalation 54 is provided with 6 ~ 8 and is evenly distributed on the circle of annular slab place; The inwall of kettle 4 is provided with multilayer cooling coil 6, and cooling coil 6 is connected with the cool cycles water inlet 14 be arranged on kettle 4 outer wall and cool cycles water out 7; The outer wall of kettle 4 is provided with heating interlayer 13, and heating interlayer 13 is connected with into heat pipe mouth 15 and goes out heat pipe mouth 8.
Charging aperture 2 and blast pipe 3 is provided with at the top of kettle 4, charging aperture 2 connects right feed pipe 16, feed pipe 16 blocks a place at charging aperture 2 upstream position, access flow adjusting device, described flow regulator comprises the liquid pump 17 connected successively, choke valve 18 and rectifier 19, a shunt pipe 20 is provided with in rectifier 19, shunt pipe 20 is provided with electromagnetic flowmeter 21, electromagnetic flowmeter 21 is fastened on the flow display device 22 of rectifier 19 outside, by arranging the shunt pipe 20 of band electromagnetic flowmeter in rectifier 19, described feed pipe 16, liquid pump 17, choke valve 18, all be tightly connected by ring flange 25 between rectifier 19, described choke valve 18 is provided with hand-operated valve wheel 23, hand-operated valve wheel 23 is in choke valve 18 symmetric position, each installation one, hand-operated valve wheel 23 is provided with reducing seal cover 24 with the connecting portion of choke valve 18, hand-operated valve wheel 23 enters the material flow of rectifier 19 for manual adjustments, the seal cover of reducing type is adopted to close, effectively can avoid the material flow after liquid pump 17 pressurizes under hyperbaric environment to the dew that exosmoses, the inside, one end that described choke valve 18 is connected with rectifier 19 is also provided with antipriming pipe and sieves 27, described rectifier 19 outer wall is provided with the open-close on-off 26 controlling electromagnetic flowmeter 21 break-make, electromagnetic flowmeter 21 can be closed when not working, in feed pipe 16, screen cloth 28 is also installed.
Material flow in feed pipe 16 pressurizes through liquid pump 17, and liquid pump, to after material flow pressurization, directly enters the shunt pipe 20 of rectifier 19 inside, under the measurement of electromagnetic flowmeter 21, can understand the uninterrupted of industrial chemicals fluid.
The side, bottom of described kettle 4 is also provided with discharging opening 9.
The utility model adopts and installs multilayer cooling coil additional at former interlayer inner wall of kettle, achieve the response function that a still can heat up simultaneously and cool, Reaction time shorten, save the required energy, having simple and compact for structure, strong and reliable advantage, is the desirable equipment of fermentation reaction; Stabilizing sleeve in the utility model and chopping disk can limit the swing of the shaft caused by fluid, chopping disk can stop the floating of container bottom input gas on the one hand, reduce ascent rate, increase gas dispersion and soak time, can shred bubble or associated media on the other hand, increase medium response area, accelerate mix and blend speed.
Above the better embodiment of this patent is explained in detail, but this patent is not limited to above-mentioned embodiment, in the ken that one skilled in the relevant art possesses, can also makes a variety of changes under the prerequisite not departing from this patent aim.
Claims (6)
1. the fermentation reaction still with flow regulator, comprise kettle, it is characterized in that, kettle top is provided with variable-frequency motor, variable-frequency motor drives the shaft connecting and extend to tank base, the bottom of shaft is connected with the fixed cover being arranged on autoclave body bottom, the shaft being positioned at kettle is evenly distributed with three layers of stirring vane, shaft between adjacent two stirring vanes is arranged one and stir stabilizer, stir stabilizer and comprise wheel hub, wheel hub be circumferentially fixed with cross blade, four blade outer rims of cross blade are arc-shaped and are in circumferentially same, cross blade is fixedly connected with the inwall of stabilizing sleeve, cross blade is located in stabilizing sleeve, stabilizing sleeve is columnar structured, the parallel equal and plane-parallel of upper and lower surface of stabilizing sleeve, chopping disk is provided with in the middle part of the outer rim of stabilizing sleeve, it is annular slab inside chopping disk, outside is for being evenly distributed on the some dentalations in the middle part of annular slab outer rim, the inwall of kettle is provided with multilayer cooling coil, cooling coil is connected with the cool cycles water inlet be arranged on kettle outer wall and cool cycles water out, the outer wall of kettle is provided with heating interlayer, heating interlayer is connected with into heat pipe mouth and goes out heat pipe mouth, charging aperture and blast pipe is provided with at the top of kettle, charging aperture connects right feed pipe, feed pipe blocks a place at charging aperture upstream position, access flow adjusting device, flow regulator comprises the liquid pump connected successively, choke valve and rectifier, a shunt pipe is provided with in rectifier, shunt pipe is provided with electromagnetic flowmeter, electromagnetic flowmeter is fastened on the flow display device of rectifier outside, by arranging the shunt pipe of band electromagnetic flowmeter in rectifier, hand-operated valve wheel is provided with reducing seal cover with the connecting portion of choke valve, hand-operated valve wheel is used for the material flow that manual adjustments enters rectifier, the inside, one end that choke valve is connected with rectifier is also provided with antipriming pipe and sieves, rectifier outer wall is provided with the open-close on-off controlling electromagnetic flowmeter break-make, electromagnetic flowmeter is in closed condition when not working, also screen cloth is installed in feed pipe.
2. the fermentation reaction still of band flow regulator according to claim 1, it is characterized in that, dentalation and annular slab one-body molded, dentalation and annular slab perpendicular, dentalation outer rim mid point is positioned on same circle and this circle place plane is parallel with stabilizing sleeve upper and lower surface, the all faceted portions of dentalation arrange R8 ~ R20 fillet, and dentalation is provided with 6 ~ 8 and is evenly distributed on the circle of annular slab place.
3. the fermentation reaction still of band flow regulator according to claim 1 and 2, is characterized in that, the top of kettle is provided with charging aperture and blast pipe.
4. the fermentation reaction still of band flow regulator according to claim 3, is characterized in that, is all connected by flangeseal between feed pipe, liquid pump, choke valve, rectifier.
5. the fermentation reaction still of the band flow regulator according to claim 1 or 2 or 4, is characterized in that, described choke valve is provided with hand-operated valve wheel, and hand-operated valve wheel, in choke valve symmetric position, respectively installs one.
6. the fermentation reaction still of band flow regulator according to claim 5, is characterized in that, the side, bottom of described kettle is also provided with discharging opening.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520454353.9U CN204768688U (en) | 2015-06-26 | 2015-06-26 | Take flow regulator's fermentation reaction cauldron |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520454353.9U CN204768688U (en) | 2015-06-26 | 2015-06-26 | Take flow regulator's fermentation reaction cauldron |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204768688U true CN204768688U (en) | 2015-11-18 |
Family
ID=54508819
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520454353.9U Expired - Fee Related CN204768688U (en) | 2015-06-26 | 2015-06-26 | Take flow regulator's fermentation reaction cauldron |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204768688U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106512793A (en) * | 2017-02-07 | 2017-03-22 | 广西大学 | Long-life chemical industrial slurry stirring treatment machine |
| CN108001876A (en) * | 2017-12-14 | 2018-05-08 | 广西庚源香料有限责任公司 | A kind of heating unit for Chemical Manufacture |
| CN109894067A (en) * | 2016-01-28 | 2019-06-18 | 乐清市拓展机械科技有限公司 | Collection temperature control with more blades and the device to stir as one |
| CN112410177A (en) * | 2020-12-03 | 2021-02-26 | 中商构能生态科技(天津)有限公司 | Fermentation tank for fermentation of whole broussonetia papyrifera |
-
2015
- 2015-06-26 CN CN201520454353.9U patent/CN204768688U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109894067A (en) * | 2016-01-28 | 2019-06-18 | 乐清市拓展机械科技有限公司 | Collection temperature control with more blades and the device to stir as one |
| CN106512793A (en) * | 2017-02-07 | 2017-03-22 | 广西大学 | Long-life chemical industrial slurry stirring treatment machine |
| CN108001876A (en) * | 2017-12-14 | 2018-05-08 | 广西庚源香料有限责任公司 | A kind of heating unit for Chemical Manufacture |
| CN112410177A (en) * | 2020-12-03 | 2021-02-26 | 中商构能生态科技(天津)有限公司 | Fermentation tank for fermentation of whole broussonetia papyrifera |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204234093U (en) | A kind of reactor for fermenting | |
| CN204768688U (en) | Take flow regulator's fermentation reaction cauldron | |
| EP2746382A1 (en) | Vortex bioreactor | |
| CN204582987U (en) | A kind of mulser | |
| CN103845926A (en) | Defoaming equipment for eliminating foams in slurry | |
| CN208414382U (en) | A kind of convenient Bioexperiment fermentor of heating | |
| CN201519578U (en) | Horizontal high-speed stirring kettle | |
| CN206521455U (en) | A kind of wine fermentation tank with agitating device | |
| CN203777722U (en) | Defoaming equipment for eliminating foam of slurry | |
| CN211394442U (en) | Fermentation tank | |
| CN205413014U (en) | Stirring device of reaction kettle | |
| CN106906124A (en) | Aeration type bioreactor | |
| CN204865802U (en) | Make things convenient for flow control's constant temperature constant speed stirred tank | |
| CN205517722U (en) | Reation kettle with waste gas recovery device | |
| CN208949284U (en) | Fermentation tank with liftable top cover | |
| CN204074085U (en) | A kind of paddle of adjusting paddle height and adopt the reactor of this paddle | |
| CN204193839U (en) | The eccentric agitator of modified form | |
| CN1994548A (en) | Fluid driven impeller stirred reactor | |
| CN207042318U (en) | Chemical machinery agitator | |
| CN205517717U (en) | Chemical reaction devices | |
| CN206549645U (en) | A kind of novel reaction kettle | |
| CN205797131U (en) | A kind of shampoo mixing and emulsifying device | |
| CN204933438U (en) | Produce the reactor equipment of MBS | |
| CN203916531U (en) | A kind of constant-temperature paint agitating device | |
| CN200963574Y (en) | Fluid driven impeller stirring type reaction device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151118 Termination date: 20180626 |