CN205392308U - Efflux mixing system - Google Patents
Efflux mixing system Download PDFInfo
- Publication number
- CN205392308U CN205392308U CN201620169342.0U CN201620169342U CN205392308U CN 205392308 U CN205392308 U CN 205392308U CN 201620169342 U CN201620169342 U CN 201620169342U CN 205392308 U CN205392308 U CN 205392308U
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- container
- jet
- water
- water pump
- agitator
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Abstract
Efflux mixing system, including water treatment facilities, water storage device is connected to water treatment facilities, and water storage device connects the jet mixing ware, and urea feed hopper is connected to one side of jet mixing ware, and the water pump is connected to the opposite side of jet mixing ware, and the agitator is connected to one side of water pump, the utility model discloses a jet mixing ware can increase stirring efficiency through the high -velocity flow as ureal agitating unit, jet mixing ware, can the heat that produces when the water pump operates at a high speed simultaneously heat 4 with mixing solution 5 the degree more is favorable to production efficiency, flash mixed and dispersion, carries out complete intimate mixing in all regions of this container to the product, and whole efflux mixing system comprises tertiary jet mixing ware, is novel stirring mode, is the technological core of this production system.
Description
Technical field
The utility model relates to a kind of stirring system, more precisely a kind of jet mixing system.
Background technology
Urea, also known as phosphoamide, the organic compound being made up of carbon, nitrogen, oxygen, hydrogen, also known as urea, is a kind of white
Look crystal.One of simplest organic compound.The diamides of carbonic acid, molecular mass 60.Mammal and some fish
The main nitrogenous end-product of class vivo protein matter metabolic breakdown.Also it is the nitrogenous fertilizer that current nitrogen content is the highest.As in one
Property fertilizer, urea is applicable to various soil and plant.It easily preserves, easy to use, and the destruction to soil is little,
It it is a kind of chemical nitrogen fertilizer that currently used amount is bigger.Industrial ammonia and carbon dioxide synthesize urine under certain condition
Element.Existing urea stirring system uses standard machinery formula stirring system mostly, and stirring efficiency is relatively low, and urea can not be very
Fast dissolving.Existing jet mixing system urea liquid after stirring can directly be discharged and come into operation, and do so is urinated
More undissolved microcrystal grain can be there is in cellulose solution.
Utility model content
The purpose of this utility model is to provide a kind of jet mixing system, it is possible to solve above-mentioned problem.
The utility model for achieving the above object, is achieved through the following technical solutions:
Jet mixing system, including water treatment facilities, water treatment facilities connect water storage device, and water storage device connects
Jet stirrer, the side of jet stirrer connects urea cast hopper, and the opposite side of jet stirrer connects water pump, water
The side of pump connects agitator, and the water inlet of agitator is connected with water pump, the delivery port of agitator and the water inlet of water pump
Connect.
In order to realize the purpose of this utility model further, it is also possible to by the following technical solutions: described agitator includes
Container, container is the cylindrical housing of upper opening, and gearbox is installed on the top of container, and gearbox is installed motor,
The output shaft of motor connects the output shaft of gearbox, and the output shaft of gearbox installs swingle, and swingle is vertical state,
The side week of swingle installs several lodicules being arranged in a row, and lodicule is the level of state, and the inwall side week of container installs several
The blade being arranged in a row, when blade and lodicule are in same plane, each blade between two adjacent lodicules,
The side, top of container is installed into water pipe and controls device, and the middle inside of container installs flow sensor, in container
Outlet pipe is installed in side, portion, controls device and connects flow sensor by wire, and the inside bottom of container installs bearing,
The outer ring of bearing is connected with container, and the inner ring of bearing is connected with the lower end of swingle.Each blade position of the present utility model
Between two adjacent lodicules, when lodicule can produce eddy current through blade in urea liquid, urea liquid is made to add
Speed rotates, so that urea minitype particle accelerates to dissolve, thus greatly reduces the microcrystal grain in urea liquid, improves
The quality of urea liquid.Outlet pipe of the present utility model is positioned at the middle part of container, can discharge treatment effect with convenient container
Best urea liquid.Flow sensor of the present utility model can sense the flow velocity of urea liquid in container, and will
Flow velocity signal is converted into the signal of telecommunication and passes to control device, controls device and controls the power output of motor according to the signal of telecommunication,
So that the urea liquid flow control in container is within the scope of suitably.Bearing of the present utility model both can facilitate
The rotation of swingle, can reduce again swingle vibration in rotary course.Gearbox of the present utility model can be adjusted
The rotating speed of joint motor.The inside bottom of described container arranges teflon coatings.Teflon coatings of the present utility model is permissible
Prevent urea granules from sticking to the bottom of container.
The utility model has the advantage of: the utility model uses jet stirrer as the agitating device of urea, jet
Agitator can increase stirring efficiency by high-velocity flow, and the heat that water pump produces when running up simultaneously can be by mixed solution
Heat 4-5 degree, be more beneficial for production efficiency, quickly mixing and dispersion, product is carried out in all regions of this container
Complete homogeneous mixing, whole jet mixing system is made up of three grades of jet stirrers, is New type agitation mode, is this
The technological core of production system.And jet stirrer does not has return loss, energy-saving efficiency is high；Do not produce suspension,
There is no sediment at the bottom of tank；Prevent whirlpool and aeration；The all parts contacted with material are made of stainless steel.This practicality
The urea liquid that novel jet stirrer exports in whipping process can be through agitator, and agitator can be by machinery
Mode urea liquid is carried out secondary agitation, make the microcrystal grain rapid solution in urea liquid, thus be greatly improved
The quality of urea liquid.After agitator stirs, the urea liquid processed can return to enter in jet stirrer
Row jet mixing again, thus improve the quality of urea liquid further.Each blade of the present utility model is positioned at adjacent
Two lodicules between, when lodicule can produce eddy current through blade in urea liquid, make urea liquid accelerate rotate,
So that urea minitype particle accelerates to dissolve, thus greatly reduce the microcrystal grain in urea liquid, improve urea liquid
Quality.Outlet pipe of the present utility model is positioned at the middle part of container, can discharge, with convenient container, the urine that treatment effect is best
Cellulose solution.Flow sensor of the present utility model can sense the flow velocity of urea liquid in container, and by flow velocity signal
It is converted into the signal of telecommunication to pass to control device, controls device and control the power output of motor according to the signal of telecommunication, so that holding
Urea liquid flow control in device is within the scope of suitably.Bearing of the present utility model both can facilitate swingle
Rotate, swingle vibration in rotary course can be reduced again.Gearbox of the present utility model can regulate motor
Rotating speed.The utility model also has advantage compact, cheap for manufacturing cost and easy to use simple for structure.
Accompanying drawing explanation
Accompanying drawing is used for providing being further appreciated by of the present utility model, and constitutes a part for specification, with this practicality
Novel embodiment is used for explaining the utility model together, is not intended that restriction of the present utility model.In the accompanying drawings:
Fig. 1 is structural representation of the present utility model；Fig. 2 is the structural representation of agitator.
Mark parts: 1 motor 2 gearbox 3 water inlet pipe 4 container 5 swingle 6 blade 7 lodicule 8 outlet pipe 9 axle
Hold 10 teflon coatings 11 flow sensors 12 and control device 13 urea cast hopper 14 jet stirrer 15 water
Pump 16 agitator 17 water treatment facilities 18 water storage device.
Detailed description of the invention
Below in conjunction with accompanying drawing, preferred embodiment of the present utility model is illustrated, it will be appreciated that described herein excellent
Select embodiment to be merely to illustrate and explain the utility model, being not used to limit the utility model.
Jet mixing system, as depicted in figs. 1 and 2, including water treatment facilities 17, water treatment facilities 17 connect water
Storage device 18, water storage device 18 connects jet stirrer 14, and the side of jet stirrer 14 connects urea and throws
Hopper 13, the opposite side of jet stirrer 14 connects water pump 15, and the side of water pump 15 connects agitator 16, stirring
The water inlet of bucket 16 is connected with water pump 15, and the delivery port of agitator 16 is connected with the water inlet of water pump 15.
The utility model uses jet stirrer 14 as the agitating device of urea, and jet stirrer 14 can be by a high speed
Current increase stirring efficiency, and mixed solution can be heated 4-5 degree, more have by the heat that water pump produces when running up simultaneously
It is beneficial to production efficiency, quickly mixing and dispersion, product is carried out complete homogeneous in all regions of this container and mixes,
Whole jet mixing system is made up of three grades of jet stirrers, is New type agitation mode, is the technology core of this production system
The heart.And jet stirrer 14 does not has return loss, energy-saving efficiency is high；Do not produce suspension, do not have sediment to exist
At the bottom of tank；Prevent whirlpool and aeration；The all parts contacted with material are made of stainless steel.Jet of the present utility model stirs
Mixing urea liquid that device 14 exports in whipping process can be through agitator 16, and agitator 16 can be by the side of machinery
Formula carries out secondary agitation to urea liquid, makes the microcrystal grain rapid solution in urea liquid, thus substantially increases urine
The quality of cellulose solution.After agitator 16 stirs, the urea liquid processed can return in jet stirrer 14
Carry out jet mixing again, thus improve the quality of urea liquid further.The original temperature of the aqueous solution be 20 degree left
The right side, urea and water mixing heat absorption become 5-10 degree, and after heating 4-5 degree, the temperature of urea liquid is 8-15 degree.
Described agitator 16 includes that container 4, container 4 are the cylindrical housing of upper opening, the top peace of container 4
Dress gearbox 2, gearbox 2 is installed motor 1, and the output shaft of motor 1 connects the output shaft of gearbox 2, speed change
The output shaft of case 2 installs swingle 5, and swingle 5 is in vertical state, and the side week installation of swingle 5 is several lines up one
The lodicule 7 of row, lodicule 7 is the level of state, and the inwall side week of container 4 installs several blades 6 being arranged in a row, when
When blade 6 and lodicule 7 are in same plane, each blade 6 between two adjacent lodicules 7, container 4
Side, top is installed into water pipe 3 and controls device 12, and the middle inside of container 4 installs flow sensor 11, container 4
Side, middle part outlet pipe 8 is installed, control device 12 and connect flow sensor 11, the inner side of container 4 by wire
Bearing 9 is installed in bottom, and the outer ring of bearing 9 is connected with container 4, and the inner ring of bearing 9 is connected with the lower end of swingle 5.
Each blade 6 of the present utility model is between two adjacent lodicules 7, when lodicule 7 is through blade 6 at urea
Eddy current can be produced in solution, make urea liquid accelerate to rotate, so that urea minitype particle accelerates to dissolve, thus significantly
Reduce the microcrystal grain in urea liquid, improve the quality of urea liquid.Outlet pipe 8 of the present utility model is positioned at container
The middle part of 4, can discharge, with convenient container 4, the urea liquid that treatment effect is best.Flow sensor of the present utility model
11 can sense the flow velocity of urea liquid in container 4, and flow velocity signal is converted into the signal of telecommunication passes to control device
12, control device 12 and control the power output of motor 1 according to the signal of telecommunication, so that the urea liquid stream in container 4
Speed controls within the scope of suitably.Bearing 9 of the present utility model both can facilitate the rotation of swingle 5, the most permissible
Reduce the swingle 5 vibration in rotary course.Gearbox 2 of the present utility model can regulate the rotating speed of motor 1.
The inside bottom of described container 4 arranges teflon coatings 10.Teflon coatings 10 of the present utility model is possible to prevent
Urea granules sticks to the bottom of container 4.
Last it is noted that the foregoing is only preferred embodiment of the present utility model, it is not limited to this
Utility model, although being described in detail the utility model with reference to previous embodiment, for the technology of this area
For personnel, the technical scheme described in foregoing embodiments still can be modified by it, or to wherein part
Technical characteristic carries out equivalent.All within spirit of the present utility model and principle, any amendment of being made, equivalent
Replacement, improvement etc., within should be included in protection domain of the present utility model.
Claims (3)
1. jet mixing system, it is characterised in that: including water treatment facilities (17), water treatment facilities (17) connect
Water storage device (18), water storage device (18) connects jet stirrer (14), and the side of jet stirrer (14) is even
Chamber pot element cast hopper (13), the opposite side of jet stirrer (14) connects water pump (15), and the side of water pump (15) connects
Agitator (16), the water inlet of agitator (16) is connected with water pump (15), the delivery port of agitator (16) and water pump (15)
Water inlet connect.
Jet mixing system the most according to claim 1, it is characterised in that: described agitator (16) includes
Container (4), container (4) is the cylindrical housing of upper opening, and gearbox (2) is installed on the top of container (4), becomes
Installing motor (1) in speed case (2), the output shaft of motor (1) connects the output shaft of gearbox (2), gearbox (2)
Output shaft installs swingle (5), and swingle (5) is in vertical state, and the side week installation of swingle (5) is several lines up one
The lodicule (7) of row, lodicule (7) is the level of state, and the inwall side week of container (4) installs several blades being arranged in a row
(6), when blade (6) is in same plane with lodicule (7), each blade (6) is positioned at adjacent two lodicule (7)
Between, the side, top of container (4) is installed into water pipe (3) and controls device (12), the middle inside peace of container (4)
Dress flow sensor (11), the side, middle part of container (4) is installed outlet pipe (8), is controlled device (12) by wire even
Connecing flow sensor (11), the inside bottom of container (4) installs bearing (9), and the outer ring of bearing (9) is with container (4) even
Connecing, the inner ring of bearing (9) is connected with the lower end of swingle (5).
Jet mixing system the most according to claim 2, it is characterised in that: at the bottom of the inner side of described container (4)
Portion arranges teflon coatings (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620169342.0U CN205392308U (en) | 2016-03-04 | 2016-03-04 | Efflux mixing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620169342.0U CN205392308U (en) | 2016-03-04 | 2016-03-04 | Efflux mixing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205392308U true CN205392308U (en) | 2016-07-27 |
Family
ID=56444149
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620169342.0U Expired - Fee Related CN205392308U (en) | 2016-03-04 | 2016-03-04 | Efflux mixing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205392308U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107051239A (en) * | 2017-03-13 | 2017-08-18 | 刘俊华 | A kind of automobile urea liquid field production device |
| CN113683103A (en) * | 2021-09-30 | 2021-11-23 | 沈阳工业大学 | Light magnesium carbonate production device and method based on resource utilization |
| CN114231737A (en) * | 2021-12-20 | 2022-03-25 | 广西汇元锰业有限责任公司 | High-pressure jet flow driving leaching device |
-
2016
- 2016-03-04 CN CN201620169342.0U patent/CN205392308U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107051239A (en) * | 2017-03-13 | 2017-08-18 | 刘俊华 | A kind of automobile urea liquid field production device |
| CN113683103A (en) * | 2021-09-30 | 2021-11-23 | 沈阳工业大学 | Light magnesium carbonate production device and method based on resource utilization |
| CN113683103B (en) * | 2021-09-30 | 2023-11-07 | 沈阳工业大学 | Light magnesium carbonate production device and method based on resource utilization |
| CN114231737A (en) * | 2021-12-20 | 2022-03-25 | 广西汇元锰业有限责任公司 | High-pressure jet flow driving leaching device |
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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 |
Granted publication date: 20160727 Termination date: 20180304 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |