CN108483541A - High-performance anti-compaction distilling apparatus - Google Patents
High-performance anti-compaction distilling apparatus Download PDFInfo
- Publication number
- CN108483541A CN108483541A CN201810325221.4A CN201810325221A CN108483541A CN 108483541 A CN108483541 A CN 108483541A CN 201810325221 A CN201810325221 A CN 201810325221A CN 108483541 A CN108483541 A CN 108483541A
- Authority
- CN
- China
- Prior art keywords
- tank body
- distillation tank
- compaction
- transmission shaft
- distilling apparatus
- 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.)
- Pending
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Classifications
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/042—Prevention of deposits
Abstract
The invention discloses a kind of high-performance anti-compaction distilling apparatus, belong to field of waste water treatment, including distillation tank body, agitating device, regional temperature monitoring device, automatic control device and automatic backflushing device, the agitating device include motor, transmission shaft and blender；The regional temperature monitoring device includes the temperature monitoring for monitoring distillation tank body bottom wall temperature；The automatic backflushing device includes recoil pump, distillation liquid case and the back flush line for putting in distillation tank interior；The automatic control device is electrically connected with temperature monitoring and recoil pump, for receiving temperature signal that temperature monitoring is sent out and controlling the start and stop of recoil pump according to distillation tank body bottom wall temperature；The high-performance anti-compaction distilling apparatus of the present invention, can be stirred the distillate inside alembic, and backwashed according to hardened situation in alembic, reach diluted effect, prevent hardened, it is ensured that distillation efficiency and saving maintenance cost.
Description
Technical field
The present invention relates to field of waste water treatment more particularly to a kind of high-performance anti-compaction distilling apparatus.
Background technology
Alembic is widely used in the industry such as chemical industry, oil, medicine, pesticide, food as common press device.
It is a kind of thermodynamic (al) separation equipment, it is different using each component boiling point in mixing liquid or liquid-solid system, makes low boiling point group
Divide evaporation, then it is the joint for evaporating and condensing two kinds of unit operations to detach the unit process of entire component to condense.
Distillation technique is widely used in the treatment of waste water, and the way of distillation can be by the moisture in waste water with the shape of vapor
Formula evaporates, and the substances such as moisture and dirty Organic substance in water is made to detach, and realizes the purification of water body, but when alembic operation, be easy
There is hardened situation, influence treatment effeciency and increases alembic maintenance cost.
Invention content
For the defects in the prior art, the present invention provides a kind of high-performance anti-compaction distilling apparatus, can be in alembic
The distillate in portion is stirred, and is backwashed according to hardened situation in alembic, and diluted effect is reached, prevent it is hardened,
Ensure distillation efficiency and saves maintenance cost.
A kind of high-performance anti-compaction distilling apparatus of the present invention, including distillation tank body, agitating device, regional temperature monitoring dress
It sets, automatic control device and automatic backflushing device, the agitating device include motor, transmission shaft and blender；The motor peace
Roof loaded on distillation tank body, the transmission shaft put in distillation tank interior from up to down, the upper end of transmission shaft and motor it is defeated
Shaft is sequentially connected, and the blender is installed on the lower end of transmission shaft；The regional temperature monitoring device includes being steamed for monitoring
Evaporate the temperature monitoring of tank body bottom wall temperature；The automatic backflushing device includes recoil pump, distills liquid case and put in distillation tank body
Internal back flush line；The automatic control device is electrically connected with temperature monitoring and recoil pump, for receiving temperature monitoring
The temperature signal that sends out and the start and stop that recoil pump is controlled according to distillation tank body bottom wall temperature；It is all provided in the transmission shaft and blender
There is recoil runner and is interconnected；The back flush line by be sleeved on the collection pendular ring outside transmission shaft with it is anti-in transmission shaft
Swash of wave road is connected to；Liquid collecting ring set is outside transmission shaft and is fixed on the end of back flush line, and collection pendular ring medial surface is equipped with annular
Collecting tank, transmission shaft are equipped with the inlet opposite with collecting tank, and inlet is communicated with the recoil runner in transmission shaft, makes recoil
Distillate in pipeline can be entered by catch basin and inlet in transmission shaft；Automatic control device device in order to control, for connecing
The signal with treatment temperature monitor feedback is received, and sends out control signal to recoil pump, when distilling tank body normal operation, bottom wall
If hardened trend occurs in subregion, local temperature will increase, and temperature monitoring will be to areas of higher temperature number at this time
According to automatic control device is fed back to, distillate is injected into recoil runner by recoil pump and back flush line, area is increased to temperature
Domain is rinsed, dilutes, and is combined to the agitating function of distillate with blender, effectively prevent distillate hardened.
Further, the temperature monitoring is equipped with multiple temperature sensors, bottom wall of each temperature sensor along distillation tank body
It is uniformly distributed；Each section temperature conditions that distillation tank body bottom wall can be monitored, when distilling the raising of tank body bottom wall local temperature, energy
It is enough accurately to monitor heating region.
Further, the blender is tooth form blender；The tooth form blender includes cross bar and is fixed on the downside of cross bar
Multiple stirrer gears, suitable for being stirred to the distillate in distillation process, and tooth form blender connects with hardened crystalline solid
Contacting surface product is small, avoids blender stuck；The shape of stirrer gear is knife-like, it is ensured that, still can be into when internal distillate is more sticky
Row stirring.
Further, the recoil runner in blender forms a spout in the downside of each stirrer gear, is set in each spout
There are one solenoid valves, and automatic control device is electrically connected the keying for controlling each solenoid valve with each solenoid valve, according to stirring
The corner of device judges stirrer gear corresponding with heating region, controls corresponding solenoid valve and opens the accurate backwash of realization,
High degree of automation, superior performance.
Further, internal viewer is additionally provided on the distillation tank body, the internal viewer is installed on distillation tank body
Roof simultaneously puts in the inside of distillation tank body, the setting observation access hole usually outside alembic, but since observation panel is in device external,
Inner case observation is unintelligible, situation is distilled from internal viewer is arranged more easily inside alembic, so as to adjust rear
Continuous process.
Further, one end that the internal viewer is put in alembic body is equipped with Fog-proof light, internal viewer with from
Dynamic control device electrical connection, internal viewer is electronics viewer, when distilling tank body normal operation, the inside observation with Fog-proof light
Device can observe alembic inner case, and internal image is fed back to automatic control device, and operating personnel can be according to prison
It controls image and carries out further work.
Further, moisture monitors are additionally provided on the distillation tank body；The moisture monitors are installed on distillation tank body
Roof and the inside for putting in distillation tank body；The moisture monitors are electrically connected with automatic control device, and existing alembic uses
Conventional time or pressure control, can not accurately control the degree of drying of waste water, moisture monitors are arranged, can will distill tank body
Interior humidity information feeds back to automatic control device, and when humidity reaches the numerical value of setting, automatic control device sends out acousto-optic report
It is alert, it prompts staff to add distillate or stops distillation, subsequent handling is carried out, after being resetted later to automatic control device
Use is can continue, to the operation of more accurate control alembic.
Further, the upper portion side wall of the distillation tank body is equipped with steam and arranges mouth, and the bottom wall for distilling tank body is arranged equipped with distillate
Put mouth.
The beneficial effects of the invention are as follows：The high-performance anti-compaction distilling apparatus of the present invention, can be to the distillation inside alembic
Liquid is stirred, and is backwashed according to hardened situation in alembic, is reached diluted effect, is prevented hardened, it is ensured that distillation
Efficiency and saving maintenance cost.
Description of the drawings
It, below will be to specific in order to illustrate more clearly of the specific embodiment of the invention or technical solution in the prior art
Embodiment or attached drawing needed to be used in the description of the prior art are briefly described.In the accompanying drawings, similar element or portion
Divide and is generally identified by similar reference numeral.In attached drawing, each element or part might not be drawn according to actual ratio.
Fig. 1 is the structural diagram of the present invention；
Fig. 2 is the vertical view of blender.
Specific implementation mode
The embodiment of technical solution of the present invention is described in detail below in conjunction with attached drawing.Following embodiment is only used for
Clearly illustrate technical scheme of the present invention, therefore be only used as example, and the protection model of the present invention cannot be limited with this
It encloses.
It should be noted that unless otherwise indicated, technical term or scientific terminology used in this application should be this hair
The ordinary meaning that bright one of ordinary skill in the art are understood.
As shown in Figure 1, 2：The high-performance anti-compaction distilling apparatus of the present embodiment, including distillation tank body 14, agitating device, area
Domain device for monitoring temperature, automatic control device 6 and automatic backflushing device, the agitating device include motor 1, transmission shaft and stirring
Device 11；The upper portion side wall of the distillation tank body 14 is equipped with steam and arranges mouth 5, and the bottom wall of distillation tank body 14 is equipped with distillate floss hole 7；
The motor 1 is installed on the roof of distillation tank body 14, and the transmission shaft is put in from up to down inside distillation tank body 14, transmission shaft
Upper end and the output shaft of motor 1 are sequentially connected, and the blender 11 is installed on the lower end of transmission shaft；The upper end of the transmission shaft with
Retarder 2 is connected between the output shaft of motor；The retarder 2 is fixedly installed in the roof of distillation tank body 14, can increase
Transmission ratio realizes the stirring of high intensity；The regional temperature monitoring device includes for monitoring distillation 14 bottom wall temperature of tank body
Temperature monitoring 4；The automatic backflushing device includes recoil pump 8, distills liquid case 9 and put in the recoil tube inside distillation tank body 14
Road；The automatic control device 6 is electrically connected with temperature monitoring 4 and recoil pump 8, the temperature sent out for receiving temperature monitoring 4
It spends signal and controls the start and stop of recoil pump 8 according to distillation 14 bottom wall temperature of tank body；It is equipped in the transmission shaft and blender 11
It recoil runner and is interconnected；The back flush line by be sleeved on the collection pendular ring 13 outside transmission shaft with it is anti-in transmission shaft
Swash of wave road is connected to；Collection pendular ring 13 is sleeved on outside transmission shaft and is fixed on the end of back flush line, and collection 13 medial surface of pendular ring is equipped with ring
The collecting tank of shape, transmission shaft are equipped with the inlet opposite with collecting tank, and inlet communicates with the recoil runner in transmission shaft, makes
Distillate in back flush line can be entered by catch basin and inlet in transmission shaft；In being additionally provided on the distillation tank body 14
Portion's viewer 15, the internal viewer 15 are installed on the roof of distillation tank body 14 and put in the inside of distillation tank body 14, usually
The setting observation access hole outside alembic, but since observation panel is in device external, inner case observation is unintelligible, and internal see is arranged
Situation is distilled from device 15 is examined more easily inside alembic, so as to adjust subsequent handling, the internal viewer 15 is put in
One end in distillation tank body 14 is equipped with Fog-proof light, and internal viewer 15 is electrically connected with automatic control device 6, internal viewer 15
For electronics viewer, when distilling 14 normal operation of tank body, the inside viewer 15 with Fog-proof light can to alembic inner case into
Row observation, and internal image is fed back into automatic control device 6, operating personnel can carry out further work according to monitoring image；
The device in order to control of automatic control device 6, the signal for receiving and treatment temperature monitor 4 is fed back, and control signal is sent out to instead
Punching pump 8, when distilling 14 normal operation of tank body, if hardened trend occurs in bottom wall portion region, local temperature will increase, this
When temperature monitoring 4 will pass through recoil pump 8 and back flush line to areas of higher temperature data feedback to automatic control device 6
Distillate is injected into recoil runner, temperature raising zone is rinsed, is diluted, with blender 11 to the stirring work(of distillate
It can be combined, effectively prevent distillate hardened.
In the present embodiment, the temperature monitoring 4 is equipped with multiple temperature sensors 16, and each temperature sensor 16 is along alembic
The bottom wall of body 14 is uniformly distributed；Each section temperature conditions that distillation 14 bottom wall of tank body can be monitored, when 14 bottom wall office of distillation tank body
When portion's temperature increases, heating region can be accurately monitored.
In the present embodiment, the blender 11 is tooth form blender；The tooth form blender includes cross bar 12 and is fixed on
Multiple stirrer gears 10 of 12 downside of cross bar, suitable for being stirred to the distillate in distillation process, and tooth form blender and plate
The crystalline solid contact area of knot is small, avoids blender 11 stuck；The shape of stirrer gear 10 be knife-like, it is ensured that internal distillate compared with
It when being sticky, can still be stirred, the recoil runner in blender 11 forms a spout in the downside of each stirrer gear 10, often
It is set in a spout there are one solenoid valve, automatic control device 6 is electrically connected with each solenoid valve for controlling opening for each solenoid valve
It closes, stirrer gear 10 corresponding with heating region is judged according to the corner of blender 11, corresponding solenoid valve is controlled and opens in fact
Now accurate backwash, high degree of automation, superior performance.
In the present embodiment, moisture monitors 3 are additionally provided on the distillation tank body 14；The moisture monitors 3 are installed on steaming
It evaporates the roof of tank body 14 and puts in the inside of distillation tank body 14；The moisture monitors 3 are electrically connected with automatic control device 6, existing
Some alembics can not accurately be controlled the degree of drying of waste water, humidity detection is arranged using conventional time or pressure control
The humidity information distilled in tank body 14 can be fed back to automatic control device 6, when humidity reaches the numerical value of setting, automatically by device 3
Control device 6 sends out sound-light alarm, and prompt staff adds distillate or stops distillation, subsequent handling is carried out, later to certainly
Dynamic control device 6 can be continuing with after being resetted, to the operation of more accurate control alembic.
Finally it should be noted that：The above embodiments are only used to illustrate the technical solution of the present invention., rather than its limitations；To the greatest extent
Present invention has been described in detail with reference to the aforementioned embodiments for pipe, it will be understood by those of ordinary skill in the art that：Its according to
So can with technical scheme described in the above embodiments is modified, either to which part or all technical features into
Row equivalent replacement；And these modifications or replacements, various embodiments of the present invention technology that it does not separate the essence of the corresponding technical solution
The range of scheme should all cover in the claim of the present invention and the range of specification.
Claims (8)
1. a kind of high-performance anti-compaction distilling apparatus, it is characterised in that：Including distillation tank body, agitating device, regional temperature monitoring
Device, automatic control device and automatic backflushing device, the agitating device include motor, transmission shaft and blender；The motor
It is installed on the roof of distillation tank body, the transmission shaft puts in distillation tank interior from up to down, the upper end of transmission shaft and motor
Output shaft is sequentially connected, and the blender is installed on the lower end of transmission shaft；The regional temperature monitoring device includes for monitoring
Distill the temperature monitoring of tank body bottom wall temperature；The automatic backflushing device includes recoil pump, distills liquid case and put in alembic
The back flush line in internal portion；The automatic control device is electrically connected with temperature monitoring and recoil pump, for receiving temperature monitoring
Temperature signal that device is sent out and the start and stop that recoil pump is controlled according to distillation tank body bottom wall temperature；In the transmission shaft and blender
Equipped with recoil runner and it is interconnected；The back flush line by the collection pendular ring that is sleeved on outside transmission shaft in transmission shaft
Recoil runner is connected to.
2. high-performance anti-compaction distilling apparatus according to claim 1, it is characterised in that：The temperature monitoring is equipped with more
A temperature sensor, each temperature sensor are uniformly distributed along the bottom wall of distillation tank body.
3. high-performance anti-compaction distilling apparatus according to claim 2, it is characterised in that：The blender stirs for tooth form
Device；The tooth form blender includes cross bar and multiple stirrer gears for being fixed on the downside of cross bar.
4. high-performance anti-compaction distilling apparatus according to claim 3, it is characterised in that：Recoil runner in blender exists
The downside of each stirrer gear forms a spout, sets that there are one solenoid valve, automatic control device and each electromagnetism in each spout
Valve is electrically connected the keying for controlling each solenoid valve.
5. high-performance anti-compaction distilling apparatus according to claim 1, it is characterised in that：It is additionally provided on the distillation tank body
Internal viewer, the internal viewer are installed on the roof of distillation tank body and put in the inside of distillation tank body.
6. high-performance anti-compaction distilling apparatus according to claim 5, it is characterised in that：The internal viewer puts in steaming
It evaporates one end in tank body and Fog-proof light is installed, internal viewer is electrically connected with automatic control device.
7. high-performance anti-compaction distilling apparatus according to claim 1, it is characterised in that：It is additionally provided on the distillation tank body
Moisture monitors；The moisture monitors are installed on the roof of distillation tank body and put in the inside of distillation tank body；The humidity prison
Device is surveyed to be electrically connected with automatic control device.
8. high-performance anti-compaction distilling apparatus according to claim 1, it is characterised in that：The upper side of the distillation tank body
Wall is equipped with steam and arranges mouth, and the bottom wall for distilling tank body is equipped with distillate floss hole.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810325221.4A CN108483541A (en) | 2018-04-12 | 2018-04-12 | High-performance anti-compaction distilling apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810325221.4A CN108483541A (en) | 2018-04-12 | 2018-04-12 | High-performance anti-compaction distilling apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108483541A true CN108483541A (en) | 2018-09-04 |
Family
ID=63315854
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810325221.4A Pending CN108483541A (en) | 2018-04-12 | 2018-04-12 | High-performance anti-compaction distilling apparatus |
Country Status (1)
| Country | Link |
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| CN (1) | CN108483541A (en) |
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Application publication date: 20180904 |
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| RJ01 | Rejection of invention patent application after publication |