CN206219464U - A kind of waste liquid recovery apparatus - Google Patents
A kind of waste liquid recovery apparatus Download PDFInfo
- Publication number
- CN206219464U CN206219464U CN201621154086.4U CN201621154086U CN206219464U CN 206219464 U CN206219464 U CN 206219464U CN 201621154086 U CN201621154086 U CN 201621154086U CN 206219464 U CN206219464 U CN 206219464U
- Authority
- CN
- China
- Prior art keywords
- reactor
- dimethylbenzene
- hexane
- methanol
- recovery
- 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
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The utility model is related to a kind of waste liquid recovery apparatus, including：Dimethylbenzene recovery system, methanol recovery system, n-hexane recovery system；Dimethylbenzene recovery system includes：Dimethylbenzene feeding device, mixing decker, dimethylbenzene reclaim reactor, dimethylbenzene collection device.Methanol recovery system includes：Methanol feed device, Methanol Recovery reactor, methanol collection device.Next station that n-hexane reclaims reactor is n-hexane collection device, and n-hexane is reclaimed and linked together using pipeline between reactor and n-hexane collection device.Wherein dimethylbenzene to be reclaimed and be respectively connected with condenser system on reactor, Methanol Recovery reactor, n-hexane recovery reactor；Condenser system is both connected in tail gas condensing system.The waste liquid recovery apparatus that the utility model is provided, three kinds of recovery of material are processed using set of system, using totally enclosed pipeline, not only recycle efficiency high, and do not pollute the environment.
Description
Technical field
The utility model is related to a kind of waste liquid recovery apparatus, and in particular to a kind of organic efficiency is high, does not have site environment
The waste liquid recovery apparatus of pollution.
Background technology
Recovery system common at present is that a kind of material is reclaimed using set of system, organic efficiency bottom, further, since work
Occasion is not closed can cause the pollution of environment.
Utility model content
Regarding to the issue above, main purpose of the present utility model is that a kind of organic efficiency of offer is high, and live ring is not had
The waste liquid recovery apparatus of border pollution.
The utility model is to solve above-mentioned technical problem by following technical proposals：A kind of waste liquid recovery apparatus, bag
Include：Dimethylbenzene recovery system, methanol recovery system, n-hexane recovery system；
Dimethylbenzene recovery system includes：Dimethylbenzene feeding device, mixing decker, dimethylbenzene reclaim reactor, diformazan
Benzene collection device；
Next station of dimethylbenzene feeding device is mixing decker, dimethylbenzene feeding device and mixing decker
Between linked together using pipeline；
Mix next station of decker for dimethylbenzene reclaims reactor, mixing decker and dimethylbenzene reclaim anti-
Answer and linked together using pipeline between kettle；
Next station that dimethylbenzene reclaims reactor is dimethylbenzene collection device, and dimethylbenzene reclaims reactor and dimethylbenzene
Linked together using pipeline between collection device；
Methanol recovery system includes：Methanol feed device, Methanol Recovery reactor, methanol collection device；
Next station of methanol feed device is Methanol Recovery reactor, methanol feed device and Methanol Recovery reactor
Between linked together using pipeline；
Next station of Methanol Recovery reactor is methanol collection device, Methanol Recovery reactor and methanol collection device
Between linked together using pipeline；
N-hexane recovery system includes：N-hexane feeding device, n-hexane reclaim reactor, n-hexane collection device；
Next station of n-hexane feeding device is that n-hexane reclaims reactor, and n-hexane feeding device and n-hexane are returned
Linked together using pipeline between receipts reactor；
Next station that n-hexane reclaims reactor is n-hexane collection device, and n-hexane reclaims reactor and n-hexane
Linked together using pipeline between collection device；
Wherein dimethylbenzene to be reclaimed and be respectively connected with condensed system on reactor, Methanol Recovery reactor, n-hexane recovery reactor
System；Condenser system is both connected in tail gas condensing system,
Retracting device is connected with mixing decker.
In specific embodiment of the utility model, dimethylbenzene reclaims reactor, Methanol Recovery reactor, n-hexane and reclaims
Retracting device is respectively connected with condenser system on reactor.
In specific embodiment of the utility model, enter at house steward's charcoal absorption through the tail gas in tail gas condensing system
Reason system.
In specific embodiment of the utility model, dimethylbenzene feeding device, methanol feed device and n-hexane charging dress
Put the pipeline for being provided with the connection of direct and house steward's activated charcoal adsorption processing system.
Positive effect of the present utility model is：The waste liquid recovery apparatus that the utility model is provided, using a set of system
System three kinds of recovery of material for the treatment of, using totally enclosed pipeline, not only recycle efficiency high, and do not pollute the environment.
Brief description of the drawings
Fig. 1 is overall structure diagram of the present utility model.
Specific embodiment
The utility model preferred embodiment is given below in conjunction with the accompanying drawings, to describe the technical solution of the utility model in detail.
Fig. 1 is overall structure diagram of the present utility model.As shown in figure 1, the devil liquor recovery dress that the utility model is provided
Put including：Dimethylbenzene recovery system, methanol recovery system, n-hexane recovery system.
Wherein, dimethylbenzene recovery system includes：Dimethylbenzene feeding device 1, mixing decker 2, dimethylbenzene reclaim reaction
Kettle 3, dimethylbenzene collection device 4.
Next station of dimethylbenzene feeding device 1 is mixing decker 2, and dimethylbenzene feeding device 1 and mixing are layered
Linked together using pipeline between device 2；Mix next station of decker 2 for dimethylbenzene reclaims reactor 3, mixing
Decker 2 and dimethylbenzene are linked together between reclaiming reactor 3 using pipeline；Dimethylbenzene reclaims the next of reactor 3
Station is dimethylbenzene collection device 4, and dimethylbenzene to be reclaimed and be connected to one using pipeline between reactor 3 and dimethylbenzene collection device 4
Rise.
Methanol recovery system includes：Methanol feed device 5, Methanol Recovery reactor 6, methanol collection device 7.
Next station of methanol feed device 5 is Methanol Recovery reactor 6, and methanol feed device 5 and Methanol Recovery are anti-
Answer and linked together using pipeline between kettle 6；Next station of Methanol Recovery reactor 6 is methanol collection device 7, and methyl alcohol is returned
Receive and linked together using pipeline between reactor 6 and methanol collection device 7；N-hexane recovery system includes：N-hexane feeds
Device 8, n-hexane reclaims reactor 9, n-hexane collection device 10.
Next station of n-hexane feeding device 8 be n-hexane reclaim reactor 9, n-hexane feeding device 8 and just oneself
Alkane is linked together between reclaiming reactor 9 using pipeline；N-hexane reclaims next station of reactor 9 for n-hexane is collected
Device 10, n-hexane is reclaimed and linked together using pipeline between reactor 9 and n-hexane collection device 10.
Wherein dimethylbenzene to be reclaimed and be respectively connected with condensation on reactor 3, Methanol Recovery reactor 6, n-hexane recovery reactor 9
System (in Fig. 1 301,601,901)；Condenser system (301,601,901) is both connected in tail gas condensing system 11, mixing point
Retracting device is connected with layer device 2.
Dimethylbenzene is reclaimed and connected in the condenser system that reactor 3, Methanol Recovery reactor 6, n-hexane are reclaimed on reactor 9
Retracting device is connected to, house steward's activated charcoal adsorption processing system is entered through the tail gas in tail gas condensing system 11.Dimethylbenzene charging dress
To put be provided with 1, methanol feed device 5 and n-hexane feeding device 8 and directly connected with house steward's activated charcoal adsorption processing system
Pipeline.
The utility model processes three kinds of recovery of material using set of system, using totally enclosed pipeline, not only at recovery
Reason efficiency high, and do not pollute the environment.
General principle of the present utility model and principal character and advantage of the present utility model has been shown and described above.One's own profession
The technical staff of industry it should be appreciated that the utility model is not restricted to the described embodiments, described in above-described embodiment and specification
Simply illustrate principle of the present utility model, on the premise of the utility model spirit and scope are not departed from, the utility model is also
Various changes and modifications are had, these changes and improvements are both fallen within the range of claimed the utility model, the utility model
Claimed scope is by appending claims and its equivalent thereof.
Claims (4)
1. a kind of waste liquid recovery apparatus, it is characterised in that：The waste liquid recovery apparatus include：Dimethylbenzene recovery system, methyl alcohol are returned
Receipts system, n-hexane recovery system；
Dimethylbenzene recovery system includes：Dimethylbenzene feeding device, mixing decker, dimethylbenzene reclaim reactor, dimethylbenzene and receive
Acquisition means；
Next station of dimethylbenzene feeding device is mixing decker, between dimethylbenzene feeding device and mixing decker
Linked together using pipeline；
Mix next station of decker for dimethylbenzene reclaims reactor, mixing decker and dimethylbenzene reclaim reactor
Between linked together using pipeline；
Next station that dimethylbenzene reclaims reactor is dimethylbenzene collection device, and dimethylbenzene reclaims reactor and dimethylbenzene is collected
Linked together using pipeline between device；
Methanol recovery system includes：Methanol feed device, Methanol Recovery reactor, methanol collection device；
Next station of methanol feed device is Methanol Recovery reactor, between methanol feed device and Methanol Recovery reactor
Linked together using pipeline；
Next station of Methanol Recovery reactor is methanol collection device, between Methanol Recovery reactor and methanol collection device
Linked together using pipeline；
N-hexane recovery system includes：N-hexane feeding device, n-hexane reclaim reactor, n-hexane collection device；
Next station of n-hexane feeding device is that n-hexane reclaims reactor, and n-hexane feeding device and n-hexane reclaim anti-
Answer and linked together using pipeline between kettle；
Next station that n-hexane reclaims reactor is n-hexane collection device, and n-hexane reclaims reactor and n-hexane is collected
Linked together using pipeline between device；
Wherein dimethylbenzene to be reclaimed and be respectively connected with condenser system on reactor, Methanol Recovery reactor, n-hexane recovery reactor；It is cold
Solidifying system is both connected in tail gas condensing system,
Retracting device is connected with mixing decker.
2. waste liquid recovery apparatus according to claim 1, it is characterised in that：It is anti-that dimethylbenzene reclaims reactor, Methanol Recovery
Answer kettle, n-hexane to reclaim in the condenser system on reactor and be respectively connected with retracting device.
3. waste liquid recovery apparatus according to claim 1, it is characterised in that：Enter total through the tail gas in tail gas condensing system
Pipe activated charcoal adsorption processing system.
4. waste liquid recovery apparatus according to claim 3, it is characterised in that：Dimethylbenzene feeding device, methanol feed device
With the pipeline that the connection of direct and house steward's activated charcoal adsorption processing system is provided with n-hexane feeding device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621154086.4U CN206219464U (en) | 2016-10-31 | 2016-10-31 | A kind of waste liquid recovery apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621154086.4U CN206219464U (en) | 2016-10-31 | 2016-10-31 | A kind of waste liquid recovery apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206219464U true CN206219464U (en) | 2017-06-06 |
Family
ID=58789065
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621154086.4U Active CN206219464U (en) | 2016-10-31 | 2016-10-31 | A kind of waste liquid recovery apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206219464U (en) |
-
2016
- 2016-10-31 CN CN201621154086.4U patent/CN206219464U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107149852B (en) | A kind for the treatment of process of volatile organic compounds containing chlorine | |
| CN203244811U (en) | Device for resourceful treatment of steel hydrochloric acid pickle liquor | |
| CN206219464U (en) | A kind of waste liquid recovery apparatus | |
| CN204079838U (en) | A kind of transesterification reaction device | |
| CN206244619U (en) | A kind of sludge treating system based on hydrothermal carbonization | |
| CN205821212U (en) | A kind of special esters of methacrylic acid tower top does not coagulates the retracting device of gas | |
| CN103130670B (en) | Synthetic leather dimethyl formamide (DMF) recycling residue processing technology and synthetic leather DMF recycling residue processing system | |
| CN201329242Y (en) | Acrylonitrile tail gas recovery device | |
| CN201862283U (en) | Extracting device for ethanediol and acetaldehyde in esterification waste gas | |
| CN109368086A (en) | A kind of underground compressed recyclable device of the not recyclable house refuse in processing city | |
| CN206188606U (en) | Vehicular sewage sludge recovery system | |
| CN211894778U (en) | Paint detects uses garbage collection device | |
| CN107445424A (en) | It is a kind of to realize the debirs thermocatalytic efficiently device of decrement and recycling | |
| CN216191999U (en) | Device for recovering methanol in production of bulk drugs | |
| CN203400518U (en) | Toluene recycling and rectifying device | |
| CN216540137U (en) | Useless salt preprocessing device of energy-concerving and environment-protective furan phenol | |
| CN205710646U (en) | A kind of diatomaceous innocuity disposal system of oil-containing | |
| CN106839655A (en) | Mobile unit and film slag drying method for treating suitable for film slag desiccation | |
| CN202263414U (en) | Tail gas recovery device | |
| CN206152567U (en) | Tail gas is retrieved and processing apparatus | |
| CN106823590A (en) | One kind mixing organic waste-gas purification and resource recovery and processing system | |
| CN203269825U (en) | DMF (dimethylfomamide) recovery residue treatment system in synthetic leather manufacturing | |
| CN210786735U (en) | Fluorescent brightener condensation reaction system | |
| CN201591996U (en) | High-temperature exhaust emission gas-liquid separation waste heat using device | |
| CN202740927U (en) | Starch dust recycling and reusing device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |