CN206700844U - A kind of continuous device for removing light component impurity - Google Patents
A kind of continuous device for removing light component impurity Download PDFInfo
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- CN206700844U CN206700844U CN201720443498.8U CN201720443498U CN206700844U CN 206700844 U CN206700844 U CN 206700844U CN 201720443498 U CN201720443498 U CN 201720443498U CN 206700844 U CN206700844 U CN 206700844U
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Abstract
It the utility model is related to a kind of continuous device for removing light component impurity.It, which includes inside, agitating shaft（3）Fluid reservoir（1）, it is characterised in that：The fluid reservoir（1）Tank body upper side is provided with light fraction outlet（2）；The agitating shaft（3）On be connected to drive rod（4）, oil scraping plate（5）；The drive rod（4）The other end be connected with push pedal（6）；The oil scraping plate（5）Lowermost end be less than the light fraction outlet（2）；The push pedal（6）Located at the oil scraping plate（5）Side.The utility model is simple in construction, easy controlled operation, and the continuous automatic removing to light component impurity in mixed system can be achieved.
Description
Technical field
It the utility model is related to the production of methyl methacrylate, more particularly to a kind of continuous dress for removing light component impurity
Put.
Background technology
Methyl methacrylate is a kind of important Organic Chemicals, and with the rising of demand, its production technology is not
Disconnected perfect, its production technology mainly includes at present：ACH methods, isobutene method and ethylene process, the ACH methods accounting 75% in, still
It is prevailing technology.The waste acid water of the light component containing organic matter can be produced during ACH methods produce methyl methacrylate, is used at present
The storage tank of agitating device is usually carried in the device for storing these waste acid waters.Light group of organic matter of spent acid water surface etc. in storage tank
Dividing impurity, the accumulation with temperature over time easily aggregates into the sticky material of asphalitine shape, and this kind of polymer viscosity is very big, and
Can because storage time is long and retrogradation is hardened.Although existing production technology is continued to optimize and improved, to light components such as asphalitines
The processing of impurity is the problem for enjoying puzzlement in the industry all the time.Processing in the industry to the light component impurity such as asphalitine at present is often
Batch (-type), solidification periodically is switched over to the asphalitine on spent acid water storage tank upper strata, artificial slag dumping cleaning, its operation is simple and crude, scene
Bad environments, and its treatment effect is bad, and then have impact on the recovery of subsequent sulphuric acid ammonium.
Utility model content
The purpose of this utility model is to provide a kind of continuous device for removing light component impurity, and its is simple in construction, operation
It is easily-controllable, the continuous automatic removing to light component impurity in mixed system can be achieved.
The purpose of this utility model is achieved through the following technical solutions：
A kind of continuous device for removing light component impurity, including the internal fluid reservoir for having agitating shaft, it is characterised in that：It is described
Liquid storage tank upper side is provided with light fraction outlet；Drive rod, oil scraping plate are connected on the agitating shaft；The driving
The other end of bar is connected with push pedal；The lowermost end of the oil scraping plate is less than the light fraction outlet；The push pedal is scraped located at described
Oiled-plate method side.
The oil scraping plate connected on agitating shaft, with the rotation of agitating shaft, realize the light components such as liquid level asphalitine is miscellaneous
Matter is gradually struck off and is deposited on oil scraping plate side, while drive rod drives push pedal to be backhauled in the side of agitating shaft along radially
It is dynamic, realize and push asphalitine on the outside of fluid reservoir to, and then cause light component impurity to discharge fluid reservoir by modes such as overflows.
As further optimization, the above-mentioned continuous device for removing light component impurity, in addition to output balance pipe and level meters；
One end of the output balance pipe connects with the bottom of above-mentioned fluid reservoir, and the bottom of the other end and above-mentioned light fraction outlet is neat
It is flat；The level meters are installed on the above-mentioned fluid reservoir at above-mentioned 4.5~5.5mm of light fraction outlet bottom.By setting out
Balance pipe and level meters are expected, to control the liquid level of the mixed system such as waste acid water in fluid reservoir to be less than light fraction outlet simultaneously, it is ensured that
Prevent the materials such as waste acid water and asphalitine from flowing out light fraction outlet together.
As further optimization, the above-mentioned continuous device for removing light component impurity, in addition to control system, the and of motor I
Motor II；The control system includes controller I, timer and controller II；The controller I, the motor I and on
Agitating shaft is stated to be sequentially connected in series；The controller II, the motor II and above-mentioned drive rod are sequentially connected in series；The timer difference
It is connected with the controller I, controller II.
As further optimization, the lowermost end of above-mentioned oil scraping plate is less than 2~4mm of bottom of above-mentioned light fraction outlet.
As further optimization, above-mentioned oil scraping plate is along stirring axial and radial distribution.
As further optimization, above-mentioned fluid reservoir side is additionally provided with observation panel；The observation panel goes out with above-mentioned light component
Mouth is in the same horizontal line.
As further optimization, above-mentioned oil scraping plate is preferably the strip groove being made up of three sides, wherein a side is vertical
In base, another side and base are in 140 °~160 ° angles；The base of the strip groove and the axial direction of above-mentioned agitating shaft are in
20 °~40 ° angles；It is located at the lower section on base in the side of 140 °~160 ° angles with base；The push pedal abuts against the bar
On the inside of the groove of connected in star.By the way that oil scraping plate is arranged into strip groove, and base tilts 20 °~40 ° and is fixed on agitating shaft, makes
Oil scraping plate is obtained under the drive of agitating shaft, the light component such as liquid level asphalitine impurity is gradually scraped, and is gradually accumulated along inclined plane
In in groove, then push pedal makes it be discharged from light fraction outlet automatically to plug-in except the asphalitine for intercepting and being deposited in groove.This
Outside, above-mentioned oil scraping plate can also use the structure setting of other conventional shapes such as V-type.
The utility model has the advantages that：
The utility model provides a kind of continuous device for removing light component impurity, and its is simple in construction, easy controlled operation, practical
Property it is strong, realize and the continuous of light component impurity in mixed system automatic removed.Wherein, the oil scraping plate connected on agitating shaft,
With the rotation of agitating shaft, realize by the light component such as liquid level asphalitine impurity gradually strike off and be deposited on oil scraping plate side or
In oil scraping plate groove, while drive rod drives and moved back and forth with radial direction of the push pedal that oil scraping plate abuts along agitating shaft, Jin Ershi
Show and pushed asphalitine on the outside of fluid reservoir to so that the light component such as asphalitine impurity discharges fluid reservoir by modes such as overflows, subtracts
Light component impurity liquid level residence time in kettle in system is lacked, has alleviated intractability, avoid artificial treatment, improved clear
Except efficiency.And further via setting up the control units such as controller I, timer, controller II so that when oil scraping plate leads to
When crossing light fraction outlet, push pedal correspondingly automatically to plug-in except light component impurity such as asphalitines, ensure that and effectively scrape.
Brief description of the drawings
Fig. 1 is the structural representation of the continuous device for removing light component impurity described in the utility model embodiment 1.
Fig. 2 is the structural representation of the continuous device for removing light component impurity described in the utility model embodiment 2.
Fig. 3 is the front view of the continuous device for removing light component impurity described in Fig. 2.
Fig. 4 is the top view of the continuous device for removing light component impurity described in Fig. 2.
Fig. 5 is the schematic diagram of fluid reservoir internal structure in the continuous device for removing light component impurity described in Fig. 2.
Fig. 6 is the right view of fluid reservoir internal structure in the continuous device for removing light component impurity described in Fig. 5.
Fig. 7 is Fig. 6 part A enlarged drawings.
Fig. 8 is the attachment structure schematic diagram of the control system in the continuous device for removing light component impurity described in Fig. 2.
Embodiment
The utility model is specifically described below by embodiment, it is necessary to it is pointed out here that be following examples
It is served only for that the utility model is further described, it is impossible to be interpreted as the limitation to scope of protection of the utility model, the field
Technical staff some nonessential modifications and adaptations can be made to the utility model according to above-mentioned the utility model content.
Embodiment 1
As shown in figure 1, a kind of continuous device for removing light component impurity, including the internal fluid reservoir 1 for being provided with agitating shaft 3；
The tank body upper side of the fluid reservoir 1 is provided with light fraction outlet 2, and tank body side is provided with charging aperture, and tank base is provided with out
Material mouth；Drive rod 4, and oil scraping plate 5 are connected on agitating shaft 3；The other end of drive rod 4 is connected with push pedal 6；Oil scraping plate
5th, in the same horizontal line, and the lowermost end of oil scraping plate 5 is less than the bottom of light fraction outlet 2 for push pedal 6 and light fraction outlet 2
3mm；Push pedal 6 is arranged at the side of oil scraping plate 5；The bottom of fluid reservoir 1 connects with one end of output balance pipe 12, output balance pipe
The top-direction of 12 other end towards fluid reservoir 1 is arranged, and is flushed with the bottom of light fraction outlet 2；Also pacify on fluid reservoir 1
Equipped with level meters 13, the level meters 13 are located at the bottom 5mm of light fraction outlet 2.
During production run, waste acid water caused by esterification enters in fluid reservoir 1 through charging aperture, and agitating shaft 3 drives entirely
Acid pickle in tank is uniformly mixed, and the asphalitine class organic polymer impurity in acid solution is fully taken to liquid level；It is fixedly connected on
Oil scraping plate 5 on agitating shaft 3, liquid level asphalitine is intercepted under the drive of agitating shaft 3, meanwhile, the push pedal being connected on drive rod 4
6 automatically to plug-in except the asphalitine for intercepting and being deposited on the side of oil scraping plate 5, and then asphalitine is discharged by way of overflow
Fluid reservoir 1, the asphalitine of discharge go incinerator to burn；The acid solution of the inner bottom part of fluid reservoir 1 discharge enters thiamine recovery through discharging opening
Device.In addition, using the principle of linker, the liquid level in fluid reservoir 1 has been monitored in real time by the output balance pipe 12 set, simultaneously
The real-time measurement of the boundary position to organic phase in tank Yu waste acid water is realized by level meters 13.
Embodiment 2
As illustrated in figs. 2 through 8, a kind of continuous device for removing light component impurity, including it is control system, motor I 10, electronic
Machine II 11 and the internal fluid reservoir 1 for being provided with agitating shaft 3；The tank body upper side of the fluid reservoir 1 is provided with light fraction outlet 2, tank body
Side is provided with charging aperture, and tank base is provided with discharging opening；It is connected to drive rod 4 on agitating shaft 3, and along stirring
The radially-arranged oil scraping plate 5 of axle 3；The other end of drive rod 4 is connected with push pedal 6；Oil scraping plate 5, push pedal 6 and light fraction outlet 2 are equal
In the same horizontal line, and oil scraping plate 5 lowermost end be less than light fraction outlet 2 bottom 4mm；Oil scraping plate 5 is by three sides
The strip groove of composition a, wherein side, perpendicular to base, another side and base are in 150 ° of angles；The base of strip groove with
The axial direction of agitating shaft 3 is in 30 ° of angles；It is located at the lower section on base in the side of 150 ° of angles with base；It is recessed that push pedal 6 abuts against bar shaped
On the inside of the groove of groove；Its control system includes controller I 7, timer 9 and controller II 8；Controller I 7 is connected with motor I 10,
Motor I 10 is also connected with agitating shaft 3；Controller II 8 is connected with motor II 11, and motor II 11 is also connected with drive rod 4；
Timer 9 is connected with controller I 7, controller II 8 respectively；The side of fluid reservoir 1 is additionally provided with observation panel, the observation panel with it is light
Component outlet 2 is in the same horizontal line.
The device of continuous removing light component impurity in this example, in production run, because the formation of asphalitine is at any time
Between, the accumulation of temperature slowly formed, so the agitating shaft 3 set speed ratio it is relatively low, be 0.5~1r/min；The He of controller I 7
The series control of controller II 8, wherein, the cycle parameter that controller I 7 records exports and is passed to controller II 8, controller II 8
The frizing cycle is adjusted according to the periodic signal of receiving, the integer doubling time frizing of agitating shaft 3 can be achieved, such as, adjust the frizing cycle
（1min）For 1 times of mixing cycle（1min）, i.e. the frizing one of oil scraping plate 5 encloses, and push pedal 6 outwards scrapes once；Adjust the frizing cycle
（1.5min）For 2 times of mixing cycles（0.75min）, i.e. the frizing two of oil scraping plate 5 encloses, and push pedal 6 outwards scrapes once；Controller II 8
The parameter value of settable regulation motor power, controllable push pedal 6 outwards scrape the speed of asphalitine.It should be noted that this is stirred
It is low to mix the rotating speed of axle 3（0.5~1min）, the initial power scope of motor II 11 is set, ensures that push pedal 6 is passed through within this range
Effectively scraping during asphalitine outlet 2.
Claims (9)
1. there is agitating shaft a kind of continuous device for removing light component impurity, including inside（3）Fluid reservoir（1）, it is characterised in that：
The fluid reservoir（1）Tank body upper side is provided with light fraction outlet（2）；The agitating shaft（3）On be connected to drive rod
（4）, oil scraping plate（5）；The drive rod（4）The other end be connected with push pedal（6）；The oil scraping plate（5）Lowermost end be less than institute
State light fraction outlet（2）；The push pedal（6）Located at the oil scraping plate（5）Side.
2. the continuous device for removing light component impurity as claimed in claim 1, it is characterised in that：It also includes output balance pipe
（12）And level meters（13）；The output balance pipe（12）One end and the fluid reservoir（1）Bottom connection, the other end and institute
State light fraction outlet（2）Bottom flush；The level meters（13）It is installed on the light fraction outlet（2）Bottom 4.5~
The fluid reservoir at 5.5mm（1）On.
3. the continuous device for removing light component impurity as claimed in claim 1 or 2, it is characterised in that：It also include control system,
Motor I（10）With motor II（11）；The control system includes controller I（7）, timer（9）With controller II（8）；
The controller I（7）, the motor I（10）With the agitating shaft（3）It is sequentially connected in series；The controller II（8）, the electricity
Motivation II（11）With the drive rod（4）It is sequentially connected in series；The timer（9）Respectively with the controller I（7）, controller II
（8）Connection.
4. the continuous device for removing light component impurity as claimed in claim 1 or 2, it is characterised in that：The oil scraping plate（5）Most
Bottom is less than the light fraction outlet（2）3~4mm of bottom；The oil scraping plate（5）Along agitating shaft（3）Radial distribution；Institute
State fluid reservoir（1）Side is additionally provided with observation panel, the observation panel and the light fraction outlet（2）In the same horizontal line.
5. the continuous device for removing light component impurity as claimed in claim 3, it is characterised in that：The oil scraping plate（5）Most bottom
End is less than the light fraction outlet（2）3~4mm of bottom；The oil scraping plate（5）Along agitating shaft（3）Radial distribution；It is described
Fluid reservoir（1）Side is additionally provided with observation panel, the observation panel and the light fraction outlet（2）In the same horizontal line.
6. the continuous device for removing light component impurity as claimed in claim 1 or 2, it is characterised in that：The oil scraping plate（5）Serve as reasons
The strip groove of three side compositions a, wherein side, perpendicular to base, another side and base are in 140 °~160 ° angles；It is described
The base of strip groove and the agitating shaft（3）Axial direction be in 20 °~40 ° angles；Side with base in 140 °~160 ° angles
Side is located at the lower section on base；The push pedal（6）On the inside of the groove for abutting against the strip groove.
7. the continuous device for removing light component impurity as claimed in claim 3, it is characterised in that：The oil scraping plate（5）For by three
The strip groove of bar side composition a, wherein side, perpendicular to base, another side and base are in 140 °~160 ° angles；The bar
The base of connected in star and the agitating shaft（3）Axial direction be in 20 °~40 ° angles；Side with base in 140 °~160 ° angles
Positioned at the lower section on base；The push pedal（6）On the inside of the groove for abutting against the strip groove.
8. the continuous device for removing light component impurity as claimed in claim 4, it is characterised in that：The oil scraping plate（5）For by three
The strip groove of bar side composition a, wherein side, perpendicular to base, another side and base are in 140 °~160 ° angles；The bar
The base of connected in star and the agitating shaft（3）Axial direction be in 20 °~40 ° angles；Side with base in 140 °~160 ° angles
Positioned at the lower section on base；The push pedal（6）On the inside of the groove for abutting against the strip groove.
9. the continuous device for removing light component impurity as claimed in claim 5, it is characterised in that：The oil scraping plate（5）For by three
The strip groove of bar side composition a, wherein side, perpendicular to base, another side and base are in 140 °~160 ° angles；The bar
The base of connected in star and the agitating shaft（3）Axial direction be in 20 °~40 ° angles；Side with base in 140 °~160 ° angles
Positioned at the lower section on base；The push pedal（6）On the inside of the groove for abutting against the strip groove.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720443498.8U CN206700844U (en) | 2017-04-25 | 2017-04-25 | A kind of continuous device for removing light component impurity |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720443498.8U CN206700844U (en) | 2017-04-25 | 2017-04-25 | A kind of continuous device for removing light component impurity |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206700844U true CN206700844U (en) | 2017-12-05 |
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ID=60457349
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720443498.8U Expired - Fee Related CN206700844U (en) | 2017-04-25 | 2017-04-25 | A kind of continuous device for removing light component impurity |
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| Country | Link |
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| CN (1) | CN206700844U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107892359A (en) * | 2017-12-15 | 2018-04-10 | 佛山高富中石油燃料沥青有限责任公司 | One kind improves Water Tank sump oil collection device |
| CN113105016A (en) * | 2021-03-31 | 2021-07-13 | 河北恒创环保科技有限公司 | Oil organic matter removing device and process in zinc extraction process in waste hydrochloric acid |
-
2017
- 2017-04-25 CN CN201720443498.8U patent/CN206700844U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107892359A (en) * | 2017-12-15 | 2018-04-10 | 佛山高富中石油燃料沥青有限责任公司 | One kind improves Water Tank sump oil collection device |
| CN113105016A (en) * | 2021-03-31 | 2021-07-13 | 河北恒创环保科技有限公司 | Oil organic matter removing device and process in zinc extraction process in waste hydrochloric acid |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171205 Termination date: 20210425 |
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| CF01 | Termination of patent right due to non-payment of annual fee |