CN205914084U - System for can control starch solution concentration - Google Patents
System for can control starch solution concentration Download PDFInfo
- Publication number
- CN205914084U CN205914084U CN201620976004.8U CN201620976004U CN205914084U CN 205914084 U CN205914084 U CN 205914084U CN 201620976004 U CN201620976004 U CN 201620976004U CN 205914084 U CN205914084 U CN 205914084U
- Authority
- CN
- China
- Prior art keywords
- dissolving tank
- starch
- pipe
- feeding
- starch solution
- 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.)
- Active
Links
Abstract
The utility model relates to a system for can control starch solution concentration, including dissolving tank and feed bin, the bottom of feed bin is equipped with ejection of compact pipeline, is equipped with interior welt on the inside wall of ejection of compact pipeline, and the bottom of ejection of compact pipeline is connected with the pay -off subassembly, and the pay -off subassembly links to each other with the dissolving tank, is connected with the inlet tube on the dissolving tank, is equipped with the stirring subassembly in the dissolving tank, is equipped with the level gauge on the dissolving tank, is connected with the conveying pipeline way on the dissolving tank, is equipped with the electric -magnetic flow meter of measurement starch solution flow on the conveying pipeline is said, calculates the flow of inlet tube through the flow of setting for electric -magnetic flow meter, the utility model discloses an advantage: the pay -off frequency that the liquid level variation that observes the dissolving tank through the level gauge adjusted the pay -off subassembly realizes the pay -off volume of control starch, and the flow through electric -magnetic flow meter calculates the flow of inlet tube water -logging, can realize that the starch and the water of stirring reaches the balance in the dissolving tank, has promoted the stability of starch concentration greatly, does not receive that starch wets, the influence of debris.
Description
Technical field
This utility model is related to a kind of system that can control starch solution concentration.
Background technology
At present, paper mill, in order to lift the quality of paper, all can increase some physical properties of paper, such as with starch
Add cationic starch in slurry, use spray starch in interlayer, use ative starch etc. in top sizing.What starch was typically bought is
Solid, powdery, and it is added on the gelatinized corn starch liquid for steaming and decocting again after dissolving having during paper machine, have plenty of the solution of starch, no matter glue
Liquid, solution require that concentration is stable, because present paper machine scale all ratios are larger, therefore typically adopt continuous starch preparation system
System, prior art is to control discharge quantity using the discharge quantity that the frequency of discharge screw controls starch, then uses electromagnetic flowmeter meter
Amount dilution water, to control the concentration of starch solution, but starch has the impact made moist, have debris in starch, starch make moist after meeting
Arch formation occurs although the generation of this phenomenon can be reduced using vibrator, but unavoidably, furthermore in starch
Debris, the debris such as rope in starch packaging bag be wound on discharge screw, discharge screw cannot accurately calculate going out of starch
Doses, therefore concentration are also unstable.
Utility model content
The technical problems to be solved in the utility model is exactly to provide a kind of system that can control starch solution concentration, solves existing
Concentration unstable problem when having starch solution dissolving.
In order to solve above-mentioned technical problem, this utility model is achieved through the following technical solutions: one kind can control shallow lake
The system of powder solution concentration, including dissolving tank and the feed bin being built-in with starch, the bottom of feed bin is provided with is easy to going out of starch discharging
Pipe material, the medial wall of discharge pipe is provided with the interior lining panel of some pieces of smooth surfaces, and the bottom of discharge pipe is connected with feeding
Assembly, feeding material component is connected with dissolving tank, receives the starch of discharge pipe discharging by feeding material component and is delivered in dissolving tank,
Water inlet pipe is connected with dissolving tank, water inlet pipe is provided with the valve controlling water inlet pipe flow and the flow of metering water inlet pipe flow
Meter, is provided with mixing component, realizes starch by mixing component and mixed with the uniform of water, and dissolving tank is provided with liquid level in dissolving tank
Meter, is changed to adjust the feeding frequency of feeding material component by the liquid level that dissolving tank observed by liquidometer, dissolving tank is connected with conveying
Pipeline, by feeding pipe, the starch solution mixing in dissolving tank is transported in subsequent processing, feeding pipe is provided with metering
The electromagnetic flowmeter of starch solution flow, calculates the flow of water inlet pipe by setting the flow of electromagnetic flowmeter.
Preferably, discharge pipe is in a back taper body setting, and discharge pipe is provided with charging aperture and discharging opening, and feeds
Mouthful and discharging opening be in eccentric setting, discharging opening is connected with connecting tube, connecting tube is connected with feeding material component, charging aperture and discharging opening
Eccentric setting can make the flow velocity difference of same outlet zones of different, and the flow velocitys of different outlets are also different simultaneously, before and after so making not
Starch with batch is mixed greatly, and the uniformity of starch is substantially improved, and starch, in flowing, does not have flow dead, starch
Uniformly decline, discharging flowing stable and uniform, improve the service life of feed bin.
Preferably, interior lining panel is welded in discharge pipe and interior lining panel is in that fish scale type is arranged, effectively avoid starch from
On down discharging when jam phenomenon occurs, be welded to connect reliability.
Preferably, feeding material component includes feed pipe, feeding spiro rod and reducing motor, and feeding spiro rod is arranged in feed pipe,
Reducing motor is connected with feeding spiro rod, and feed pipe is provided with the charging hole matching with connecting tube, and feed pipe is provided with discharge opening,
Discharge nozzle is connected with discharge opening, discharge nozzle is connected with dissolving tank, and electromagnetic flowmeter is connected with reducing motor, by reducing motor
The rotating speed controlling feeding spiro rod realizes the adjustable of feeding frequency, and realizes the discharging of starch by discharge opening, the setting of discharge nozzle,
Can guarantee that starch can fully enter in dissolving tank, decrease the waste of starch.
Preferably, mixing component includes lid and puddler, and lid snaps onto on dissolving tank, and puddler is rotatably connected on lid
On body, puddler is connected with motor, motor is fixedly connected on lid, the setting of lid, when can prevent from stirring, solution flies
Splash, mixing effect is good, structure is simple, easy installation and removal.
Preferably, feeding pipe includes conveying pipeline and dehvery pump, and dehvery pump is arranged on conveying pipeline realizes starch solution
Conveying, conveying effect is good, reliable and stable, prevents the blocking of feeding pipe.
Preferably, feed bin includes cylinder and top cover, and top cover is detachably connected with cylinder, and top cover is provided with venthole, gives vent to anger
Permeability cell is connected with hole, the diameter of described venthole is not less than the internal diameter of permeability cell, realizes cylinder by venthole and permeability cell
The balance of internal air pressure, top cover is detachably connected with cylinder, is easy to the feed supplement of starch, the setting of venthole and permeability cell, can protect
The balance of card cylinder internal gas pressure, can effectively prevent material negative pressure in blanking process middle cylinder body excessive, be easy to starch discharging.
Preferably, permeability cell is arranged on venthole by union joint, connects reliable, easy installation and removal, air permeable effect
Good.
Preferably, cylinder is provided with the continuous way level-sensing device of starch material position in detection cylinder, can guarantee that starch in cylinder
Without interruption, realize the seriality producing.
In sum, advantage of the present utility model: 1. change to adjust feeding by the liquid level that dissolving tank observed by liquidometer
The feeding frequency of assembly is realized controlling the feeding amount of starch, calculates the stream of water in water inlet pipe by the flow of electromagnetic flowmeter
Amount, enables the starch of stirring and water in dissolving tank and reaches balance, greatly improve the stability of starch concentration, be not subject to by starch
Tide, the impact of debris；
2. the setting of discharge pipe, can guarantee that the starch in feed bin is delivered in feeding material component, and the setting of interior lining panel can carry
Efficiency during high starch discharging, prevents starch from blocking in discharge pipe；
3. the setting of feeding material component, can be accurately controlled the feeding amount of starch, reach optimal starch solution；
4. the setting of mixing component, can guarantee that the uniform mixing of starch and water, improves the quality of starch solution；
5. the valve that water inlet pipe is provided with enables the control of water inlet pipe flow, and measures the stream of water inlet pipe by effusion meter
Amount, accurately can be controlled to the flow of water, realize dissolving tank inner equilibrium.
Brief description
The utility model is described in further detail below in conjunction with the accompanying drawings:
Fig. 1 is a kind of structural representation of the system that can control starch solution concentration of this utility model；
Fig. 2 is the structural representation of this utility model discharge pipe；
Fig. 3 is the structural representation of this utility model interior lining panel；
Fig. 4 is the structural representation of this utility model feeding material component；
Fig. 5 is the structural representation of this utility model mixing component；
Fig. 6 is the partial schematic diagram of this utility model feed bin.
Specific embodiment
As shown in Figure 1, Figure 2, shown in Fig. 3, Fig. 4, Fig. 5, Fig. 6, a kind of system that can control starch solution concentration, including dissolving tank
1 and be built-in with the feed bin 2 of starch, the bottom of feed bin 2 is provided with the discharge pipe 3 being easy to starch discharging, the medial wall of discharge pipe 3
It is provided with the interior lining panel 30 of some pieces of smooth surfaces, the bottom of discharge pipe 3 is connected with feeding material component 4, feeding material component 4 and dissolving
Groove 1 is connected, and receives the starch of discharge pipe 3 discharging by feeding material component 4 and is delivered in dissolving tank 1, dissolving tank 1 is connected with
Water inlet pipe 5, water inlet pipe 5 is provided with the valve 51 controlling water inlet pipe 5 flow and the effusion meter 52 of metering water inlet pipe 5 flow, dissolving
It is provided with mixing component 6 in groove 1, starch is realized by mixing component 6 and mixes with the uniform of water, and dissolving tank 1 is provided with liquidometer
11, changed to adjust the feeding frequency of feeding material component 4 by the liquid level that dissolving tank 1 observed by liquidometer 11, dissolving tank 1 is connected with
Feeding pipe 7, by feeding pipe 7, the starch solution of mixing in dissolving tank 1 is transported in subsequent processing, on feeding pipe 7
It is provided with the electromagnetic flowmeter 70 of metering starch solution flow, calculate water inlet pipe 5 by setting the flow of electromagnetic flowmeter 70
Flow.
Discharge pipe 3 is in a back taper body setting, and discharge pipe 3 is provided with charging aperture 31 and discharging opening 32, and feeds
Mouth 31 and discharging opening 32 are in eccentric setting, discharging opening 32 are connected with connecting tube 33, connecting tube 33 is connected with feeding material component 4, enters
Material mouth and discharging opening eccentric setting can make that the flow velocity of same outlet zones of different is different, and the different flow velocitys exporting are also different simultaneously,
The starch so making before and after's different batches is mixed greatly, and the uniformity of starch is substantially improved, and starch, in flowing, does not have stream
Dynamic dead band, starch uniformly declines, discharging flowing stable and uniform, improves the service life of feed bin, interior lining panel 30 is welded on discharging
Pipeline 3 is interior and interior lining panel 30 is in that fish scale type is arranged, and jam phenomenon, welding when effectively avoiding starch discharging from top to bottom
Connect reliable.
Feeding material component 4 includes feed pipe 41, feeding spiro rod 42 and reducing motor 43, and feeding spiro rod 42 is arranged on feed pipe 41
Interior, reducing motor 43 is connected with feeding spiro rod 42, and feed pipe 41 is provided with the charging hole 40 matching with connecting tube 33, feed pipe
41 are provided with discharge opening 44, and discharge opening 44 is connected with discharge nozzle 45, and discharge nozzle 45 is connected with dissolving tank 1, electromagnetic flowmeter 70
It is connected with reducing motor 43, the adjustable of feeding frequency is realized by the rotating speed that reducing motor controls feeding spiro rod, and pass through discharging
The discharging of starch, the setting of discharge nozzle are realized in hole, can guarantee that starch can fully enter in dissolving tank, decrease the waste of starch,
Mixing component 6 includes lid 61 and puddler 62, and lid 61 snaps onto on dissolving tank 1, and puddler 62 is rotatably connected on lid 61
On, puddler 62 is connected with motor 63, motor 63 is connected with puddler 62 by worm and gear, and motor 63 is fixedly connected on lid
On body 61, the setting of lid, the splashing of solution when can prevent from stirring, mixing effect is good, and structure is simple, and easy installation and removal is defeated
Pipe material 7 includes conveying pipeline 71 and dehvery pump 72, and dehvery pump 72 is arranged on the conveying realizing starch solution on conveying pipeline 71, conveying
Effect is good, reliable and stable, prevents the blocking of feeding pipe.
Feed bin 2 includes cylinder 21 and top cover 22, and top cover 22 is detachably connected with cylinder 21, and top cover 22 is provided with venthole
23, venthole 23 is connected with permeability cell 24, the diameter of described venthole 23 is not less than the internal diameter of permeability cell 24, by venthole
23 and permeability cell 24 realize the balance of cylinder 21 internal gas pressure, top cover is detachably connected with cylinder, is easy to the feed supplement of starch, venthole
With the setting of permeability cell, can guarantee that the balance of cylinder internal gas pressure, can effectively prevent material negative pressure in blanking process middle cylinder body
Excessive, it is easy to starch discharging, permeability cell 24 is arranged on venthole 23 by union joint 25, connect reliable, easy installation and removal,
Air permeable effect is good, and cylinder 21 is provided with the continuous way level-sensing device 26 of starch material position in detection cylinder, can guarantee that starch in cylinder
Without interruption, realize the seriality producing.
During use, the starch in feed bin is entered in feeding material component 4 by discharge pipe 3, by feeding material component 4 by starch
It is delivered in dissolving tank 1, then calculates the flow of water inlet pipe 5 by setting the flow of electromagnetic flowmeter 70, and pass through valve
51 and effusion meter 52 realize the precise control of water inlet pipe 5 flow, operator pass through to observe liquidometer 11, then form sediment when liquid level declines
Powder load is little, increases the feeding frequency of feeding material component 4, greatly, reduces sending of feeding material component 4 when liquid level rises then starch load
Material frequency, is made the starch in dissolving tank 2 reach balance with water, and lid 61 is snapped onto on dissolving tank 1, driven by motor 63
Puddler 62 makes starch and water uniform stirring, and the starch solution after stirring is transported to next work by dehvery pump 72 through conveying pipeline 71
In sequence.
In addition to above preferred embodiment, this utility model also has other embodiments, and those skilled in the art can root
It is variously modified according to this utility model and deforms, without departing from spirit of the present utility model, this utility model all should be belonged to
Scope defined in claims.
Claims (9)
1. a kind of system that can control starch solution concentration it is characterised in that: include dissolving tank (1) and the feed bin that is built-in with starch
(2), the bottom of feed bin (2) is provided with the discharge pipe (3) being easy to starch discharging, and the medial wall of discharge pipe (3) is provided with some
The interior lining panel (30) of block smooth surface, the bottom of discharge pipe (3) is connected with feeding material component (4), feeding material component (4) and dissolving tank
(1) it is connected, the starch of discharge pipe (3) discharging is received by feeding material component (4) and is delivered in dissolving tank (1), dissolving tank (1)
On be connected with water inlet pipe (5), water inlet pipe (5) be provided with control water inlet pipe (5) flow valve (51) and metering water inlet pipe (5) flow
The effusion meter (52) of amount, is provided with mixing component (6) in dissolving tank (1), realize uniformly mixing of starch and water by mixing component (6)
Close, and dissolving tank (1) is provided with liquidometer (11), sent to adjust by the liquid level change that dissolving tank (1) observed by liquidometer (11)
The feeding frequency of material assembly (4), dissolving tank (1) is connected with feeding pipe (7), by feeding pipe (7) by dissolving tank (1)
The starch solution of mixing is transported in subsequent processing, and feeding pipe (7) is provided with the electromagnetic flowmeter of metering starch solution flow
(70) flow of water inlet pipe (5), is calculated by setting the flow of electromagnetic flowmeter (70).
2. a kind of system that can control starch solution concentration according to claim 1 it is characterised in that: discharge pipe (3)
Arrange in a back taper body, discharge pipe (3) is provided with charging aperture (31) and discharging opening (32), and charging aperture (31) and discharging
Mouth (32) is in eccentric setting, discharging opening (32) is connected with connecting tube (33), connecting tube (33) is connected with feeding material component (4).
3. a kind of system that can control starch solution concentration according to claim 1 and 2 it is characterised in that: interior lining panel
(30) it is welded in discharge pipe (3) and interior lining panel (30) is in that fish scale type is arranged.
4. a kind of system that can control starch solution concentration according to claim 2 it is characterised in that: feeding material component (4)
Including feed pipe (41), feeding spiro rod (42) and reducing motor (43), feeding spiro rod (42) is arranged in feed pipe (41), slows down
Motor (43) is connected with feeding spiro rod (42), and feed pipe (41) is provided with the charging hole (40) matching with connecting tube (33), send
Expects pipe (41) is provided with discharge opening (44), and discharge opening (44) is connected with discharge nozzle (45), discharge nozzle (45) and dissolving tank (1) phase
Even, electromagnetic flowmeter (70) is connected with reducing motor (43).
5. a kind of system that can control starch solution concentration according to claim 1 it is characterised in that: mixing component (6)
Including lid (61) and puddler (62), lid (61) snaps onto on dissolving tank (1), and puddler (62) is rotatably connected on lid
(61) on, puddler (62) is connected with motor (63), motor (63) is fixedly connected on lid (61).
6. a kind of system that can control starch solution concentration according to claim 1 it is characterised in that: feeding pipe (7)
Including conveying pipeline (71) and dehvery pump (72), dehvery pump (72) is arranged on the conveying realizing starch solution on conveying pipeline (71).
7. a kind of system that can control starch solution concentration according to claim 1 it is characterised in that: feed bin (2) include
Cylinder (21) and top cover (22), top cover (22) is detachably connected with cylinder (21), and top cover (22) is provided with venthole (23), gives vent to anger
Permeability cell (24) is connected with hole (23), the diameter of described venthole (23) is not less than the internal diameter of permeability cell (24), by giving vent to anger
Hole (23) and permeability cell (24) realize the balance of cylinder (21) internal gas pressure.
8. a kind of system that can control starch solution concentration according to claim 7 it is characterised in that: permeability cell (24) lead to
Cross union joint (25) to be arranged on venthole (23).
9. a kind of system that can control starch solution concentration according to claim 7 it is characterised in that: cylinder sets on (21)
There is the continuous way level-sensing device (26) of starch material position in detection cylinder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620976004.8U CN205914084U (en) | 2016-08-28 | 2016-08-28 | System for can control starch solution concentration |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620976004.8U CN205914084U (en) | 2016-08-28 | 2016-08-28 | System for can control starch solution concentration |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205914084U true CN205914084U (en) | 2017-02-01 |
Family
ID=57868954
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620976004.8U Active CN205914084U (en) | 2016-08-28 | 2016-08-28 | System for can control starch solution concentration |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205914084U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106110948A (en) * | 2016-08-28 | 2016-11-16 | 浙江景兴纸业股份有限公司 | A kind of system that can control starch solution concentration |
| CN113830877A (en) * | 2021-10-18 | 2021-12-24 | 上海上禹环保科技有限公司 | Automatic chlorination device for sewage pretreatment |
| CN113929203A (en) * | 2021-10-18 | 2022-01-14 | 上海上禹环保科技有限公司 | Sewage pretreatment system |
-
2016
- 2016-08-28 CN CN201620976004.8U patent/CN205914084U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106110948A (en) * | 2016-08-28 | 2016-11-16 | 浙江景兴纸业股份有限公司 | A kind of system that can control starch solution concentration |
| CN113830877A (en) * | 2021-10-18 | 2021-12-24 | 上海上禹环保科技有限公司 | Automatic chlorination device for sewage pretreatment |
| CN113929203A (en) * | 2021-10-18 | 2022-01-14 | 上海上禹环保科技有限公司 | Sewage pretreatment system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205914084U (en) | System for can control starch solution concentration | |
| CN206924747U (en) | Full-automatic reactor charging water-adding system | |
| CN103726821B (en) | Acidizing and fracturing fluid continuous mixture feeder | |
| CN208035013U (en) | Automatic mixing pulping system | |
| CN106110948A (en) | A kind of system that can control starch solution concentration | |
| CN109879570A (en) | Bottom-mud dewatering desiccation Optimal Control System | |
| CN109879571A (en) | Bottom-mud dewatering desiccation optimal control method | |
| CN207012857U (en) | One kind production glass tube automatic recipe maker | |
| CN212167083U (en) | Weighing type feed additive agitating unit | |
| CN210905789U (en) | Universal automatic preparation device for solid and liquid medicaments | |
| CN209901125U (en) | A constant speed liquid feeding stirred tank for coating production | |
| CN207862417U (en) | Zinc powder feeding device for wet zinc-making system | |
| CN207225718U (en) | A kind of liquid automatic loading system | |
| CN214136688U (en) | High-efficient high-speed vortex pulping machine | |
| CN202666733U (en) | Batching device for coater | |
| CN210699674U (en) | Brewing device for powdery amphoteric dry strength agent | |
| CN206965697U (en) | A kind of scattered Dropping feeder | |
| CN205635023U (en) | Flocculating agent automatic reagent feeding system | |
| CN111420586A (en) | Carbon slurry feeding device and feeding method thereof | |
| CN107068965B (en) | Full-automatic production line of pipeline formula battery thick liquids | |
| CN207313103U (en) | A kind of ink filling apparatus | |
| CN218755208U (en) | Water injection dilution system | |
| CN205965714U (en) | Water -soluble fertile production line of liquid | |
| CN209348599U (en) | A kind of mixing charging reaction kettle preparing beneficiation reagent | |
| CN209065495U (en) | Flocculant prepares automatically and throwing device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |