CN207708578U - A kind of organic solvent recovery device - Google Patents
A kind of organic solvent recovery device Download PDFInfo
- Publication number
- CN207708578U CN207708578U CN201721500712.5U CN201721500712U CN207708578U CN 207708578 U CN207708578 U CN 207708578U CN 201721500712 U CN201721500712 U CN 201721500712U CN 207708578 U CN207708578 U CN 207708578U
- Authority
- CN
- China
- Prior art keywords
- tank body
- pipe
- baffle
- blow
- mixing liquid
- 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.)
- Expired - Fee Related
Links
- 239000003960 organic solvent Substances 0.000 title claims abstract description 19
- 238000011084 recovery Methods 0.000 title claims abstract description 19
- 239000007788 liquid Substances 0.000 claims abstract description 34
- 238000002156 mixing Methods 0.000 claims abstract description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 11
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims description 72
- 238000001816 cooling Methods 0.000 claims description 18
- 238000004064 recycling Methods 0.000 abstract description 5
- 239000002904 solvent Substances 0.000 abstract description 5
- 230000003139 buffering effect Effects 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 7
- 239000011344 liquid material Substances 0.000 description 4
- 238000013517 stratification Methods 0.000 description 4
- 239000010865 sewage Substances 0.000 description 3
- 235000020535 bottled fortified water Nutrition 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 238000001727 in vivo Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000004080 punching Methods 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model provides a kind of organic solvent recovery device, including tank body, the top of tank body is equipped with inlet and exhaust outlet, mixing liquid is entered by inlet in tank body, the gas generated in mixing liquid tank body is discharged by exhaust outlet, the cross section of tank body is equipped with baffle, the outer edge of baffle and the madial wall of tank body connect, offered on baffle it is multiple for mixing liquid and gas by through-hole, the side wall of tank body is equipped with oil exit pipe and blow-off pipe, oil exit pipe and blow-off pipe are located at the lower section of baffle, blow-off pipe is located at the bottom of tank wall, oil discharge outlet is located at the top of blow-off pipe, a drainpipe is additionally provided in tank body, the other end that one end of drainpipe extends to the interior bottom discharge pipe of tank body is located at the outside of tank body.Mixing liquid enters via baffle in tank body from inlet, and is layered in tank body, and upper layer oil is discharged by oil exit pipe, and lower water is discharged by drainpipe, is achieved in the recycling of solvent.Baffle plays the role of a buffering to the mixing liquid entered in tank body and uniformly dispenses, and prevents mixing liquid to be poured into tank body and causes security risk.
Description
Technical field
The utility model belongs to retracting device field, the solvent recovery being more particularly in a kind of punching pump for fortified water
Device.
Background technology
Benzene smell is excessive when existing flush-type vacuum pump work in the market, in addition pump housing running generates temperature, benzene concentration
It is excessively high to calculate a danger source in chemical industry.Therefore, the device that the solvent in the existing punching pump for fortified water is recycled is being pacified
It is badly in need of improving in full performance.
Utility model content
The purpose of this utility model is to provide that a kind of leakproofness is preferable and the preferable organic solvent recovery device of security performance.
A purpose according to the present utility model, provides a kind of organic solvent recovery device, including tank body,
The top of the tank body is equipped with inlet, and mixing liquid is entered by inlet in tank body, tank described in mixing liquid
The gas generated in vivo is discharged by exhaust outlet,
The cross section of the tank body is equipped with baffle, and the outer edge of the baffle is connect with the madial wall of the tank body, institute
The middle part for stating baffle is equipped with groove, is equipped with the inlet tube for extending to the bottom portion of groove at the inlet, the baffle it is recessed
Offered on slot it is multiple for mixing liquid and gas by through-hole,
The side wall of the tank body is equipped with oil exit pipe and blow-off pipe, and the oil exit pipe and the blow-off pipe are located at the baffle
Lower section, the blow-off pipe is located at the bottom of the tank wall, and the oil discharge outlet is located at the top of the blow-off pipe, the tank
Be additionally provided with a drainpipe in vivo, one end of the drainpipe extends to the interior bottom of the tank body, the drainpipe it is another
End is located at the outside of the tank body,
Spiral cooling coil is equipped in the tank body, the spiral cooling coil is located at the top of the baffle, the spiral shell
The water inlet pipe of rotation cooling coil extends to the outside of the tank body across the side wall of the tank body, and the spiral cooling coil goes out
Water pipe extends to the outside of the tank body across the side wall of the tank body.
Mixing liquid enters via the through-hole of inlet tube and blind recess in tank body from inlet, and is layered in tank body,
Upper layer oil is discharged by oil exit pipe, and lower water is discharged by drainpipe, is achieved in the recycling of solvent；Cooling water from water inlet pipe into
Enter spiral cooling coil, be discharged by outlet pipe, benzene vapour of the spiral cooling coil for generating in cooling tank body makes its liquefaction be
Liquid is recovered in tank body.Baffle plays the role of a buffering to the mixing liquid entered in tank body and uniformly dispenses,
It prevents mixing liquid to be poured into tank body and causes security risk.
In some embodiments, it is additionally provided with exhaust outlet at the top of the tank body.Tank body passes through exhaust outlet and waste gas recovery
Device is connected to, and steam pressure is excessive when preventing the benzene vapour in tank body from can not liquefy completely, causes security risk.
In some embodiments, the tank body is connect by exhaust pipe with benzene receiving tank.Due to containing in mixing liquid
Benzene, the exhaust outlet of the present apparatus and the emission-control equipment in downstream connect, and thus can prevent benzene leakage from causing environmental protection and safety problem.
In some embodiments, the oil exit pipe is equipped with oil extraction valve.It is possible thereby to control the switch of oil exit pipe.
In some embodiments, the blow-off pipe is equipped with sewage draining valve.When being cleaned to tank body, blowdown valve is opened
Goalkeeper's blow-off pipe is opened, and drains the liquid of tank body, personnel easy to operation clean it.
A kind of organic solvent recovery method using organic solvent recovery device,
Liquid material is entered via the inlet tube in the groove of the baffle by the inlet；
Stratification after liquid material in the groove of the baffle is mixed by through-hole with the water in the tank body；
The steam benzene that the spiral cooling coil generates after being divided into is condensed into liquid benzene；
Liquid benzene is discharged by the oil exit pipe obtained by the liquid benzene of stratification acquisition in the tank body and condensation,
Collect organic solvent.
Thus benzene is subjected to whole recycling, avoids polluting caused by the discharge of gas benzene or after-treatment, reduction is produced into
This.
Description of the drawings
Fig. 1 is a kind of structural schematic diagram of the organic solvent recovery device of embodiment of utility model.
Specific implementation mode
Fig. 1 schematically shows a kind of organic solvent recovery device of embodiment of the utility model.Such as Fig. 1 institutes
Show, the organic solvent recovery device, including tank body 1.
The top of tank body 1 is equipped with inlet 11 and exhaust outlet 12.Mixing liquid is entered by inlet 11 in tank body 1.It is mixed
The gas that liquid generates in tank body 1 is closed to be discharged by exhaust outlet 12.The cross section of tank body 1 is equipped with baffle 2.The outside of baffle 2
Edge is connect with the madial wall of tank body 1.The middle part of baffle 2 is equipped with groove 22, offer on groove 22 it is multiple for mixing liquid and
Gas by through-hole 21.Inlet tube 111 is equipped at inlet 11, inlet tube 111 extends to the bottom of groove 22.Tank body 1
Side wall is equipped with oil exit pipe 13 and blow-off pipe 14, and oil exit pipe 13 and blow-off pipe 14 are located at the lower section of baffle 2, and blow-off pipe 14 is located at tank
The bottom of 1 side wall of body, oil discharge outlet are located at the top of blow-off pipe 14, are additionally provided with a drainpipe 15 in tank body 1, and the one of drainpipe 15
The other end for the interior bottom discharge pipe 15 for extending to tank body 1 is held to be located at the outside of tank body 1.Mixing liquid is from inlet 11 via gear
Plate 2 enters in tank body 1, and the layering in tank body 1, upper layer oil are discharged by oil exit pipe 13, and lower water is discharged by drainpipe 15,
It is achieved in the recycling of solvent.Spiral cooling coil 3 is equipped in tank body 1.Spiral cooling coil 3 is located at the top of baffle 2, spiral
The water inlet pipe 31 of cooling coil 3 extends to the outside of tank body 1 across the side wall of tank body 1, and the outlet pipe 32 of spiral cooling coil 3 is worn
The side wall for crossing tank body 1 extends to the outside of tank body 1.Cooling water enters spiral cooling coil 3 from water inlet pipe 31, by 32 row of outlet pipe
Go out, spiral cooling coil 3 is used to cool down the benzene vapour generated in tank body 1, and it is that liquid is recovered in tank body 1 to make its liquefaction.Gear
Plate 2 plays the role of a buffering and uniformly dispenses to entering the mixing liquid in tank body 1, and mixing liquid is prevented to be poured into tank
Body 1 causes security risk.Tank body 1 is connect by exhaust pipe with benzene receiving tank.Due to containing benzene, the row of the present apparatus in mixing liquid
Gas port 12 is connect with the emission-control equipment in downstream, thus can prevent benzene leakage from causing environmental protection and safety problem.On oil exit pipe 13
Equipped with oil extraction valve 131.It is possible thereby to control the switch of oil exit pipe 13.Blow-off pipe 14 is equipped with sewage draining valve 141.To tank body 1
When being cleaned, opens sewage draining valve 141 and open blow-off pipe 14, drain the liquid of tank body 1, personnel easy to operation carry out it
Cleaning.
A kind of organic solvent recovery method using organic solvent recovery device：Liquid material by inlet 11 via into
Liquid pipe 111 enters in the groove 22 of baffle 2；Liquid material in the groove 22 of baffle 2 is mixed by the water in through-hole 21 and tank body 1
Stratification after conjunction；The steam benzene that spiral cooling coil 3 generates after being divided into is condensed into liquid benzene；Stratification in tank body 1
Liquid benzene obtained by the liquid benzene of acquisition and condensation is discharged by oil exit pipe 13, collects organic solvent.Thus benzene is carried out all
Recycling, pollution or after-treatment caused by avoiding the discharge of gas benzene, reduces production cost.
The above are merely some embodiments of the utility model.For those of ordinary skill in the art, it is not taking off
Under the premise of the concept of the present invention, various modifications and improvements can be made, these belong to the utility model
Protection domain.
Claims (5)
1. a kind of organic solvent recovery device, which is characterized in that including tank body,
The top of the tank body is equipped with inlet, and mixing liquid is entered by inlet in tank body, in tank body described in mixing liquid
The gas of generation is discharged by exhaust outlet,
The cross section of the tank body is equipped with baffle, and the outer edge of the baffle is connect with the madial wall of the tank body, the gear
The middle part of plate is equipped with groove, is equipped with the inlet tube for extending to the bottom portion of groove at the inlet, on the groove of the baffle
Offer it is multiple for mixing liquid and gas by through-hole,
The side wall of the tank body is equipped with oil exit pipe and blow-off pipe, and the oil exit pipe and the blow-off pipe are located under the baffle
Side, the blow-off pipe are located at the bottom of the tank wall, and the blow-off pipe is located at the lower section of oil discharge outlet, is also set in the tank body
There are one drainpipe, one end of the drainpipe extends to the interior bottom of the tank body, and the other end of the drainpipe is located at institute
The outside of tank body is stated,
Spiral cooling coil is equipped in the tank body, the spiral cooling coil is located at the top of the baffle, and the spiral is cold
But the water inlet pipe of coil pipe extends to the outside of the tank body, the outlet pipe of the spiral cooling coil across the side wall of the tank body
The outside of the tank body is extended to across the side wall of the tank body.
2. organic solvent recovery device according to claim 1, which is characterized in that be additionally provided with exhaust at the top of the tank body
Mouthful.
3. organic solvent recovery device according to claim 1, which is characterized in that the tank body is connect by exhaust pipe and benzene
Closed cans connects.
4. organic solvent recovery device according to claim 1, which is characterized in that the oil exit pipe is equipped with draining valve
Door.
5. organic solvent recovery device according to claim 1, which is characterized in that the blow-off pipe is equipped with blowdown valve
Door.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721500712.5U CN207708578U (en) | 2017-11-10 | 2017-11-10 | A kind of organic solvent recovery device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721500712.5U CN207708578U (en) | 2017-11-10 | 2017-11-10 | A kind of organic solvent recovery device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207708578U true CN207708578U (en) | 2018-08-10 |
Family
ID=63061222
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721500712.5U Expired - Fee Related CN207708578U (en) | 2017-11-10 | 2017-11-10 | A kind of organic solvent recovery device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207708578U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107626117A (en) * | 2017-11-10 | 2018-01-26 | 大丰鑫源达化工有限公司 | A kind of organic solvent recovery device |
| CN109135808A (en) * | 2018-09-21 | 2019-01-04 | 叶锦程 | A kind of integrated form dewatering processing device for petroleum crude oil refining |
-
2017
- 2017-11-10 CN CN201721500712.5U patent/CN207708578U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107626117A (en) * | 2017-11-10 | 2018-01-26 | 大丰鑫源达化工有限公司 | A kind of organic solvent recovery device |
| CN109135808A (en) * | 2018-09-21 | 2019-01-04 | 叶锦程 | A kind of integrated form dewatering processing device for petroleum crude oil refining |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104001702B (en) | Gas station's sunken tankers mechanical cleaning system | |
| CN105152374B (en) | Full-automatic food garbage solid-liquid and water-oil separating lifting discharge efficient process system | |
| CN207708578U (en) | A kind of organic solvent recovery device | |
| CN109665606B (en) | Sewage treatment device | |
| CN104746638B (en) | Powerful sludge slag-liquid separation car | |
| CN205606194U (en) | Coal gas drainer convenient to clearance | |
| CN206033307U (en) | A deoiling machine for sewage treatment | |
| CN107626117A (en) | A kind of organic solvent recovery device | |
| CN204767613U (en) | Compressor oil recovery device that gives up | |
| CN205957756U (en) | Mixed steam spray cooling tower of profit and mixed steam cooling device of sled dress formula profit | |
| CN208218590U (en) | A kind of machining oil-containing waste water treating device | |
| CN205560770U (en) | Environmental protection and energy saving pyrolysis device | |
| CN201028271Y (en) | Natural gas steam trap with drawer type filter | |
| CN109454095A (en) | It is a kind of for source pretreatment after kitchen castoff feed bin | |
| CN212425761U (en) | Biological medical treatment effluent treatment purifier | |
| CN203586178U (en) | Drain and blowdown water recovery device | |
| CN210302498U (en) | Spice extracting and concentrating device | |
| CN207451678U (en) | A kind of bath sewage treatment box | |
| CN201625493U (en) | Device for recycling waste tire discomposed oil gas | |
| CN206366255U (en) | A kind of corrosion-resistant anti-clogging spiral-flow type steam-water separator | |
| CN205586743U (en) | Gas treatment device | |
| CN107661642A (en) | A kind of full automatic grease separator | |
| CN201121141Y (en) | Environment friendly oil stain separating-cleaning reclamation plant | |
| CN203297169U (en) | Siphon negative pressure waste liquor recoverer | |
| CN208372650U (en) | A kind of pipeline raffinate collection tapping equipment |
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: 20180810 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |