CN206705877U - The retracting device of aromatic compound in a kind of organic wastewater - Google Patents
The retracting device of aromatic compound in a kind of organic wastewater Download PDFInfo
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- CN206705877U CN206705877U CN201720163653.0U CN201720163653U CN206705877U CN 206705877 U CN206705877 U CN 206705877U CN 201720163653 U CN201720163653 U CN 201720163653U CN 206705877 U CN206705877 U CN 206705877U
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- evaporator
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Abstract
The utility model discloses a kind of retracting device of aromatic compound in organic wastewater, wastewater disposal basin delivery port connects primary filter water inlet by pipeline, primary filter delivery port pipeline connects evaporator water inlet, pipeline is provided with the first water pump between primary filter and evaporator, base of evaporator is provided with electric heater unit, evaporator sidewall upper connects condenser pipe one end by inverted u-shaped pipeline, the condenser pipe other end connects collector, collector top connects vavuum pump by pipeline, evaporator delivery port connects the water inlet of BAF by pipeline, the delivery port of BAF passes through connecting pipe of pipeline formula film filter water inlet, tubular type film filter water outlet pipe road connects collecting-tank, connecting pipe between tubular type film filter and collecting-tank is provided with the second water pump.The utility model is simple in construction, easy to use, and recovering effect is good, and operating efficiency is high, and waste water treatment process is smooth.
Description
Technical field
The utility model belongs to aromatic compound in technical field of sewage treatment equipment, more particularly to a kind of organic wastewater
Retracting device.
Background technology
The wastewater treatment of chemical technology field obtains significant progress by development for many years at present, on waste water recycling,
Wastewater treatment has reached a suitable level.Wherein COD processing is both emphasis and difficult point, traditional processing method there is
The problems such as handling process is long, floor space is big, effluent quality does not reach reuse requirement, in the prior art with film bio-separation skill
The combination of art and membrane filtration and active sludge biological method, has obtained significant progress.However, in the prior art, produced for chemical industry
Product manufacturing enterprise, especially essence and flavoring agent manufacturing enterprise, its waste water is typically by directly handling, wherein the aromatic compound contained
Recycling can not be recycled, causes the waste of product, and has aggravated intractability, is unfavorable for the raising of economic benefit.And
In processing procedure, if the impurity such as particulate matter is more larger in waste water, the efficiency of follow-up membrane filtration is influenced whether, or even will
Membrane filter system blocks, break treat with equipment.
It is those skilled in that art's skill urgently to be resolved hurrily therefore, because above-mentioned technological deficiency in the prior art be present
Art problem.
Utility model content
Retracting device of the purpose of this utility model in the aromatic compound in a kind of organic wastewater is provided, it is intended to solve existing
There is present in technology in chemical products waste water aromatic compound to be recycled to cause to waste, and particulate matter in waste water
The problem of considerable influence equipment is run.
What the utility model was realized in：
The retracting device of aromatic compound in a kind of organic wastewater, including wastewater disposal basin, primary filter, the first water pump, steaming
Hair device, electric heater unit, condenser pipe, collector, vavuum pump, BAF, tubular type film filter, the second water pump, catchment
Pond and control valve, the wastewater disposal basin delivery port connect primary filter water inlet, the primary filter water outlet by pipeline
Mouth pipeline connection evaporator water inlet, pipeline is provided with the first water pump, the evaporation between the primary filter and evaporator
Device bottom is provided with electric heater unit, and the evaporator sidewall upper connects condenser pipe one end, the condensation by inverted u-shaped pipeline
The pipe other end connects collector, and the collector top connects vavuum pump by pipeline, and the evaporator delivery port passes through pipeline
The water inlet of BAF is connected, the delivery port of the BAF is intake by connecting pipe of pipeline formula film filter
Mouthful, the tubular type film filter water outlet pipe road connects collecting-tank, the connecting tube between the tubular type film filter and collecting-tank
Road is provided with the second water pump, the wastewater disposal basin, primary filter, evaporator, BAF, tubular type film filter and catchments
Control valve is equipped between pond on pipeline.
Preferably, the evaporator is provided with two and is arranged in parallel, and the U-shaped pipe and condenser pipe are also respectively equipped with two
Set, the U-shaped pipe are provided with control valve.
Preferably, agitating device is provided with the evaporator, control panel, the steaming is fixed with the evaporator outer wall
Electronic thermometer is inserted with hair device side wall, the control panel electrically connects the electronic thermometer and electric heater unit.
Preferably, the primary filter includes casing, primary filter net and blow-off pipe, and the casing middle part is transversal to be provided with
Primary filter net, the casing water inlet are located at primary filter side off the net, and the casing delivery port is located at the casing top
End, the bottom half is taper, and the bottom half conical lower portion is provided with blow-off pipe.
Preferably, the condenser pipe blocks up including sleeve pipe, vertical tube and water conservancy diversion, and described sleeve pipe upper and lower ends are equipped with water conservancy diversion and blocked up,
Multiple vertical tubes be arrangeding in parallel are provided between two water conservancy diversion are stifled, described sleeve pipe side wall upper and lower ends are respectively equipped with going out for cooling water
The mouth of a river and water inlet.
The beneficial effects of the utility model are：By setting evaporator is related to recovery to set in the front end of wastewater treatment
It is standby, the aromatic compound in spices and essence enterprise wastewater from chemical industry can be made to be volatilized, and carried out by condenser pipe and collector
Recovery, it is achieved thereby that the recycling of aromatic compound；And primary filter is provided with after wastewater disposal basin, can be to useless
Larger particles etc. carry out stop removal in water, reduce the operation burden of follow-up membrane filter system.The utility model is simple in construction,
Easy to use, recovering effect is good, and operating efficiency is high, and waste water treatment process is smooth.
Brief description of the drawings
Fig. 1 is the utility model structure diagram；
Fig. 2 is the structural representation of primary filter of the present utility model；
Fig. 3 is the structural representation of condenser pipe of the present utility model；
In figure：1 wastewater disposal basin；2 primary filters；201 casings；202 primary filter nets；203 blow-off pipes；3 first water pumps；4
Evaporator；5 electric heater units；6 condenser pipes；601 sleeve pipes；602 vertical tubes；603 water conservancy diversion block up；7 collectors；8 vavuum pumps；9 aeration lifes
Thing filter tank；10 tubular type film filters；11 second water pumps；12 collecting-tanks；13 control valves；14U type pipelines；15 agitating devices；16
Control panel；17 electronic thermometers.
Embodiment
In order that the purpose of this utility model, technical scheme and advantage are more clearly understood, below in conjunction with accompanying drawing and implementation
Example, the utility model is further elaborated.It should be appreciated that specific embodiment described herein is only explaining
The utility model, it is not used to limit the utility model.
Fig. 1 to 3 shows the retracting device of aromatic compound in a kind of organic wastewater of the present utility model, including wastewater disposal basin
1st, primary filter 2, the first water pump 3, evaporator 4, electric heater unit 5, condenser pipe 6, collector 7, vavuum pump 8, aeration and biological
Filter tank 9, tubular type film filter 10, the second water pump 11, collecting-tank 12 and control valve 13, wastewater disposal basin 1 delay as the storage of waste water
Equipment is rushed, the waste water discharged from factory floor can be collected.The delivery port of wastewater disposal basin 1 connects primary mistake by pipeline
The water inlet of filter 2, primary filter 2 can carry out primary filtration to waste water, mainly by larger particles in waste water
Solid is filtered out, and prevents it from entering in follow-up sewage treatment equipment.The delivery port pipeline of primary filter 2 connection
The water inlet of evaporator 4, pipeline is provided with the first water pump 3 between the primary filter 2 and evaporator 4, can by the first water pump 3
Waste water in primary filter 2 is pumped into evaporator 4.The bottom of evaporator 4 is provided with electric heater unit 5, electrical heating dress
Put 5 water bodys that can be in evaporator 4 to be heated, the aromatic compound for making wherein to contain improves volatilization effect, the evaporator 4
Sidewall upper connects the one end of condenser pipe 6 by inverted u-shaped pipeline 14, and the other end of condenser pipe 6 connects collector 7, the receipts
The top of storage 7 connects vavuum pump 8 by pipeline, when in use, by the inlet channel and outlet conduit control valve of the both sides of evaporator 4
Door 13 is closed, and so as to make evaporator 4 be in relatively independent state, now opens vavuum pump 8 and evaporator 4 take out very
Sky, the volatilization efficiency of aromatic compound can be promoted, aromatic compound is cooled down by condenser pipe 6 after volatilizing, with steam one
Rise and liquefy and collected by collector 7.The delivery port of evaporator 4 connects the water inlet of BAF 9, aeration by pipeline
Biofilter 9 belongs to sewage treatment equipment commonly used in the art, and purchase use can be carried out from commercially available prod.The aeration life
The delivery port in thing filter tank 9 is filtered by the water inlet of connecting pipe of pipeline formula film filter 10, tubular type film filter 10 by Rigid Porous
Medium form micron filter equipment, can 0.5 μm -100 μm or so of disposable filtering viscous thin material, can obtain filtrate clarification
Filter effect, belong to sewage treatment equipment commonly used in the art, purchase use can be carried out from commercially available prod.The tubular type
The delivery port pipeline of film filter 10 connects collecting-tank 12, on the connecting pipe between the tubular type film filter 10 and collecting-tank 12
Provided with the second water pump 11, it is that waste water provides power by tubular type film filter 10 by the second water pump 11, conveniently makes by filtering
Water body enter in collecting-tank 12.The wastewater disposal basin 1, primary filter 2, evaporator 4, BAF 9, tubular membrane mistake
Control valve 13 is equipped between filter 10 and collecting-tank 12 on pipeline.
Further, the evaporator 4 is provided with two and is arranged in parallel, and the U-shaped pipe 14 and condenser pipe 6 are also distinguished
Provided with two sets, collector 7 (not embodied in Fig. 1) respectively connected.The U-shaped pipe 14 is provided with control valve 13.By setting
Two evaporators 4 are put, so as to the recovery operation of alternately aromatic compound.Specifically, carried out first to an evaporator 4
Supply water, after water supply terminates, by control valve 13 by the both sides closedown of pipeline of evaporator 4, start to start electric heater unit 5, true
Empty pump 8 and condenser pipe 6, heating volatilization is carried out to the aromatic compound in waste water；It can be waved in said one evaporator 4 in heating
During hair-like state, another is in into water state, and after the completion of water to be entered, above-mentioned evaporator 4 discharges its interior water body, continues to intake,
Now another evaporator 4 entered after water then carries out heating volatilization work, it is achieved thereby that two evaporators 4 can be alternately
Work, substantially increase the organic efficiency of aromatic compound.
Further, agitating device 15 is provided with the evaporator 4, chain of command is fixed with the outer wall of evaporator 4
Plate 16, electronic thermometer 17 is inserted with the side wall of evaporator 4, the control panel 16 electrically connects the electronic thermometer 17
With electric heater unit 5.Specifically, the stirring motor of agitating device 15 is arranged on the outer top of evaporator 4, agitating paddle is arranged on steaming
Send out in the casing 201 of device 4, stirring motor drive connection agitating paddle, under the stirring action of agitating device 15, it makes to enter evaporation
Waste water in device 4 is mixed, the rate of volatilization of enhancing wherein aromatic compound.
Further, the primary filter 2 includes casing 201, primary filter net 202 and blow-off pipe 203, the case
The middle part of body 201 is transversal to be provided with primary filter net 202, and the water inlet of casing 201 is located at the lower section of primary filter net 202, institute
State the delivery port of casing 201 and be located at the top of casing 201, the bottom of casing 201 is taper, the bottom pyramidal of casing 201
Bottom is provided with blow-off pipe 203.The mesh number of primary filter net 202 can be selected as needed, and it is commercially available that in the market may be selected
Stainless steel filter screen is used, and the sewage being passed through mainly is had to pass through primary filter net 202 and entered by its operation principle upwards
Row filtering could be discharged from the upper end of casing 201, and the larger particles in waste water are then intercepted and dropped to by primary filter net 202
Conical lower portion, in use for some time, controllable blow-off pipe 203, which is opened, is discharged intercepted larger particles.And pass through
The wastewater fraction after primary filter net 202 filters is crossed then to discharge from the delivery port of the upper end of casing 201 and enter steaming by pipeline
Send out in device 4.
Further, the condenser pipe 6 includes sleeve pipe 601, vertical tube 602 and water conservancy diversion stifled 603, and described sleeve pipe is about 601
Both ends are equipped with water conservancy diversion stifled 603, and multiple vertical tubes 602 be arrangeding in parallel, described sleeve pipe 601 are provided between two water conservancy diversion stifled 603
Side wall upper and lower ends are respectively equipped with the delivery port and water inlet of cooling water.Sleeve pipe 601 is connected through a screw thread with U-shaped pipe 14,
Convenient dismounting, water conservancy diversion stifled 603 are the closure plates of elastomeric material, which is provided with the hole worn for vertical tube 602, two water conservancy diversion stifled 603 it
Between be fixed with multiple vertical tubes 602 so that the gas in U-shaped pipe 14 is cooled down by vertical tube 602, without causing gas
It is leaked in sleeve pipe 601, and the gas in volatilization makes by vertical tube 602, it is cold by being passed through in cooling water intake phase sleeve pipe 601
But water, cooling water is made to cool vertical tube 602, so that the aromatic compound of volatilization obtains cooling recovery.
Operation principle of the present utility model is as follows：
Enter in wastewater disposal basin 1 and collected from the waste water of chemical enterprise factory discharge, led to waste water by connecting pipe
Entering into primary filter 2, waste water is passed through primary filter net 202, the wherein solid impurity of bulky grain will be got rid of by filtering,
And the water body after being filtered then is discharged from the delivery port of the upper end of primary filter 2, and on pipeline the first water pump 3 effect
Under, waste water is further entered in evaporator 4, and two evaporators 4 are arranged in parallel, and can be used alternatingly.Wherein evaporate
The use principle of device 4 is as follows：
After water body enters the amount specified in evaporator 4, the control valve 13 on inlet channel and outlet conduit is controlled
Close, now electric heater unit 5 is controlled by the control panel 16 on evaporator 4, the water body being in evaporator 4
Heated, and by the temperature of water body in the real time measure evaporator 4 of electronic thermometer 17, and temperature data real-time display is existed
On control panel 16, the agitating device 15 that is arranged on evaporator 4 can be stirred to water body in evaporator 4, improve water body
Degree of being heated evenly, when water temperature reaches 50 DEG C or so in evaporator 4, control vavuum pump 8 is opened, and evaporator 4 is vacuumized,
The steam of volatilization and aromatic compound in evaporator 4 are drawn into U-shaped pipe 14 and entered further into condenser pipe 6, is made
Aromatic compound is condensed, and is collected in collector 7.After certain time is collected, vavuum pump 8 can be closed, and will steam
Control valve 13 is opened on the inlet channel and outlet conduit of hair device 4 both sides, the water body in it is flowed into BAF 9
In handled, and carry out subsequent treatment.And two evaporators 4 can alternately evaporate work, realize fragrance to be arranged in parallel
The lasting recovery of compound, improve operating efficiency.
And water body enters BAF 9 and carries out Air Exposure, then by the active force of the second water pump 11, make water
Body enters further into from BAF 9 carries out further filtration treatment in tubular type film filter 10, and will finally locate
The water body of reason is entered further into collecting-tank 12.
The beneficial effects of the utility model are：By setting evaporator 4 related to recovery in the front end of wastewater treatment
Equipment, the aromatic compound in spices and essence enterprise wastewater from chemical industry can be made to be volatilized, and pass through condenser pipe 6 and collector 7
Reclaimed, it is achieved thereby that the recycling of aromatic compound；And it is provided with primary filter 2, energy after wastewater disposal basin 1
It is enough that stop removal is carried out to larger particles in waste water etc., reduce the operation burden of follow-up membrane filter system.The utility model knot
Structure is simple, easy to use, and recovering effect is good, and operating efficiency is high, and waste water treatment process is smooth.
It is not new to this practicality although above-mentioned specific embodiment of the present utility model is described with reference to accompanying drawing
The limitation of type protection domain, one of ordinary skill in the art should be understood that on the basis of the technical solution of the utility model, ability
Field technique personnel would not require any inventive effort the various modifications that can be made or deformation still in protection of the present utility model
Within the scope of.
Claims (5)
- A kind of 1. retracting device of aromatic compound in organic wastewater, it is characterised in that：Including wastewater disposal basin, primary filter, One water pump, evaporator, electric heater unit, condenser pipe, collector, vavuum pump, BAF, tubular type film filter, second Water pump, collecting-tank and control valve, the wastewater disposal basin delivery port connect primary filter water inlet, the primary mistake by pipeline Filter delivery port pipeline connects evaporator water inlet, and pipeline is provided with the first water pump between the primary filter and evaporator, The base of evaporator is provided with electric heater unit, and the evaporator sidewall upper connects condenser pipe one end by inverted u-shaped pipeline, The condenser pipe other end connects collector, and the collector top connects vavuum pump, the evaporator delivery port by pipeline The water inlet of BAF is connected by pipeline, the delivery port of the BAF passes through connecting pipe of pipeline formula film mistake Filter water inlet, the tubular type film filter water outlet pipe road connects collecting-tank, between the tubular type film filter and collecting-tank Connecting pipe be provided with the second water pump, the wastewater disposal basin, primary filter, evaporator, BAF, tubular type membrane filtration Control valve is equipped between device and collecting-tank on pipeline.
- 2. the retracting device of aromatic compound in organic wastewater as claimed in claim 1, it is characterised in that：The evaporator is set There are two and be arranged in parallel, the U-shaped pipe and condenser pipe are also respectively equipped with two sets, and the U-shaped pipe is provided with control valve.
- 3. the retracting device of aromatic compound in organic wastewater as claimed in claim 2, it is characterised in that：In the evaporator Provided with agitating device, control panel is fixed with the evaporator outer wall, electronic thermometer is inserted with the evaporator side wall, The control panel electrically connects the electronic thermometer and electric heater unit.
- 4. the retracting device of aromatic compound in organic wastewater as claimed in claim 3, it is characterised in that：The primary filter Device includes casing, primary filter net and blow-off pipe, and the casing middle part is transversal to be provided with primary filter net, and the casing water inlet is set In primary filter side off the net, the casing delivery port is located at the casing top, and the bottom half is taper, the case Body bottom pyramidal bottom is provided with blow-off pipe.
- 5. the retracting device of aromatic compound in the organic wastewater as any one of Claims 1-4, it is characterised in that： The condenser pipe blocks up including sleeve pipe, vertical tube and water conservancy diversion, and described sleeve pipe upper and lower ends are equipped with water conservancy diversion and blocked up, between two water conservancy diversion are stifled Provided with multiple vertical tubes be arrangeding in parallel, described sleeve pipe side wall upper and lower ends are respectively equipped with the delivery port and water inlet of cooling water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720163653.0U CN206705877U (en) | 2017-02-23 | 2017-02-23 | The retracting device of aromatic compound in a kind of organic wastewater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720163653.0U CN206705877U (en) | 2017-02-23 | 2017-02-23 | The retracting device of aromatic compound in a kind of organic wastewater |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206705877U true CN206705877U (en) | 2017-12-05 |
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ID=60469087
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720163653.0U Expired - Fee Related CN206705877U (en) | 2017-02-23 | 2017-02-23 | The retracting device of aromatic compound in a kind of organic wastewater |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206705877U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109991063A (en) * | 2019-04-25 | 2019-07-09 | 广西壮族自治区药用植物园 | The paraffin section method of Paris polyphylla root tuber |
| CN114573132A (en) * | 2022-03-15 | 2022-06-03 | 山东维天精细化工科技有限公司 | Recovery unit of aromatic compound in organic waste water |
-
2017
- 2017-02-23 CN CN201720163653.0U patent/CN206705877U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109991063A (en) * | 2019-04-25 | 2019-07-09 | 广西壮族自治区药用植物园 | The paraffin section method of Paris polyphylla root tuber |
| CN114573132A (en) * | 2022-03-15 | 2022-06-03 | 山东维天精细化工科技有限公司 | Recovery unit of aromatic compound in organic waste water |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171205 Termination date: 20210223 |