CN215822683U - Closed collecting and processing system for VOCs (volatile organic compounds) in furfural slag discharge process - Google Patents
Closed collecting and processing system for VOCs (volatile organic compounds) in furfural slag discharge process Download PDFInfo
- Publication number
- CN215822683U CN215822683U CN202122486196.8U CN202122486196U CN215822683U CN 215822683 U CN215822683 U CN 215822683U CN 202122486196 U CN202122486196 U CN 202122486196U CN 215822683 U CN215822683 U CN 215822683U
- Authority
- CN
- China
- Prior art keywords
- room
- vocs
- furfural
- subside
- cyclone
- 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
Images
Landscapes
- Cyclones (AREA)
Abstract
The utility model relates to the field of furfural chemical industry, in particular to a furfural deslagging VOCs closed collecting and processing system. Sediment belt conveyor (3) have been arranged to the below of cyclone (2), sediment belt conveyor (3) can remove the solid sediment of separating, mixed air inlet (1) has been arranged on cyclone (2), gas outlet (4) have been arranged to cyclone (2) top, second grade clean system (5) are being connected in gas outlet (4), second grade clean system (5) are being connected trachea (6) once more through the pipeline, trachea (6) once more lead to whole clean room (9) that deposit room (7) and subside isolation room (10) constitute jointly, contain the partition wall between deposit room (7) and the subside isolation room (10), it is gaseous processing connecting pipe (11) of VOCS to stretch out the pipeline on subside isolation room (10).
Description
Technical Field
The utility model relates to the field of furfural chemical industry, in particular to a furfural deslagging VOCs closed collecting and processing system.
Background
In the furfural production process, aldehyde steam produced by a hydrolysis kettle can bring out part of powdery furfural residues, and when the aldehyde steam enters a primary distillation tower for distillation, the furfural residues are gradually accumulated in the tower, so that the operation of the distillation tower is greatly influenced, the distillation effect is slightly influenced, the tower is stopped if the aldehyde steam is heavy, and the furfural causes great trouble to the production.
Secondly, in the traditional furfural production, aldehyde steam is generally filled in a pressure tank by magnetic rings, tiles and the like to be used as a filtering device, but the method is troublesome in cleaning and replacing the magnetic rings, and the magnetic rings or the tiles cannot be recycled after being used, so that a large amount of solid waste is generated.
SUMMERY OF THE UTILITY MODEL
The purpose of the utility model is that: in order to provide a furfural residue-discharging VOCs closed collecting and processing system with better effect, the specific purpose is to see a plurality of substantial technical effects of the specific implementation part.
In order to achieve the purpose, the utility model adopts the following technical scheme:
the utility model provides a sediment VOCs is airtight to be collected processing system is arranged to furfural, a serial communication port, sediment belt conveyor 3 has been arranged to cyclone 2's below, sediment belt conveyor 3 can move away the solid sediment that separates, mixed air inlet 1 has been arranged on cyclone 2, gas outlet 4 has been arranged to cyclone 2 top, gas outlet 4 is connecting second grade clean system 5, second grade clean system 5 is connecting trachea 6 once more through the pipe connection, trachea 6 once more leads to the whole clean room 9 that the subsides room 7 and subside isolation room 10 constitute jointly, contain the partition wall between subsides room 7 and the subside isolation room 10, it is connecting VOCS gas treatment connecting pipe 11 to stretch out the pipeline on the subside isolation room 10.
The further technical scheme of the utility model is that a filtering device is arranged in the secondary purification system 5.
The further technical scheme of the utility model is that a spraying purification device is arranged in the secondary purification system 5.
The further technical scheme of the utility model is that a bottom waste water storage area 8 is arranged below the settling chamber 7, and the waste water storage area 8 is connected with a dilute acid configuration device through a pipeline.
The utility model has the further technical scheme that a wastewater tank 12 is arranged at the right side of the integral purification chamber 9, and the wastewater tank 12 is connected with a sewage treatment area through a water pump.
Compared with the prior art, the utility model adopting the technical scheme has the following beneficial effects: the gas enters the mixed gas inlet 1, then is separated in the cyclone separator, the gas outlet 4 carries part of solid, the part of solid enters the secondary purification system 5 for further purification, finally enters the settling chamber 7 for settling, the solid settling is realized, and finally enters the VOCS gas treatment connecting pipe 11 for gas treatment.
Drawings
To further illustrate the present invention, further description is provided below with reference to the accompanying drawings:
FIG. 1 is a schematic structural view of the utility model;
wherein: 1. a mixing gas inlet; 2. a cyclone separator; 3. a slag belt conveyor; 4. a gas outlet; 5. a secondary purification system; 6. then, the trachea is performed again; 7. a settling chamber; 8. a bottom wastewater containment area; 9. an integral purification chamber; 10. a settling isolation chamber; a VOCS gas treatment connection pipe; 12. a wastewater tank;
Detailed Description
The present invention will be further illustrated with reference to the accompanying drawings and specific embodiments, which are to be understood as merely illustrative of the utility model and not as limiting the scope of the utility model. In the description of the present invention, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", "top", "bottom", and the like indicate orientations or positional relationships based on those shown in the drawings, and are only for convenience of description and simplicity of description, but do not indicate or imply that the referred device or element must have a specific orientation, be constructed in a specific orientation, and be operated, and thus, should not be construed as limiting the present invention. Furthermore, unless expressly stated or limited otherwise, the terms "mounted," "connected," and "connected" are to be construed broadly, as they may be fixedly connected, detachably connected, or integrally connected, for example; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meanings of the above terms in the present invention can be understood in specific cases to those skilled in the art.
It is noted that, herein, relational terms such as first and second, and the like may be used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Also, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus.
The patent provides a plurality of parallel schemes, and different expressions belong to an improved scheme based on a basic scheme or a parallel scheme. Each solution has its own unique features. In addition, the technical features involved in the different embodiments of the present invention described below may be combined with each other as long as they do not conflict with each other. The fixing means, which is not described herein, may be any one of screw fixing, bolt fixing, or glue bonding.
The first embodiment is as follows: in conjunction with FIG. 1; the utility model provides a sediment VOCs is airtight to be collected processing system is arranged to furfural, a serial communication port, sediment belt conveyor 3 has been arranged to cyclone 2's below, sediment belt conveyor 3 can move away the solid sediment that separates, mixed air inlet 1 has been arranged on cyclone 2, gas outlet 4 has been arranged to cyclone 2 top, gas outlet 4 is connecting second grade clean system 5, second grade clean system 5 is connecting trachea 6 once more through the pipe connection, trachea 6 once more leads to the whole clean room 9 that the subsides room 7 and subside isolation room 10 constitute jointly, contain the partition wall between subsides room 7 and the subside isolation room 10, it is connecting VOCS gas treatment connecting pipe 11 to stretch out the pipeline on the subside isolation room 10. The technical scheme of the utility model has the following substantial technical effects and the realization process: the gas enters the mixed gas inlet 1, then is separated in the cyclone separator, the gas outlet 4 carries part of solid, the part of solid enters the secondary purification system 5 for further purification, finally enters the settling chamber 7 for settling, the solid settling is realized, and finally enters the VOCS gas treatment connecting pipe 11 for gas treatment.
Example two: as a further development or in parallel or alternatively independently, the secondary purification system 5 is internally provided with a filtration device. The technical scheme of the utility model has the following substantial technical effects and the realization process: the filtering device can further realize solid filtering.
Example three: as a further development or in parallel or alternatively independently, a spray cleaning device is provided inside the secondary cleaning system 5. The technical scheme of the utility model has the following substantial technical effects and the realization process: the spray purification device can spray to properly treat gas and solid.
Example four: as a further development or a parallel development or an alternative independent development, a bottom waste water storage region 8 is arranged below the settling chamber 7, and the waste water storage region 8 is connected to the dilute acid configuration device via a pipeline.
Example five: as a further development or in parallel or alternatively independently, a waste water basin 12 is arranged on the right side of the overall cleaning chamber 9, the waste water basin 12 being connected to the sewage treatment zone by means of a water pump.
Whole clean room 9 disposes cooling system, and this cooling system is water-cooled tube or refrigerant cold tube, and water-cooled tube or refrigerant cold tube walk in the wall of whole clean room 9, reduce whole temperature, because the temperature is too high, and gas is difficult for subsiding, and the molecular activity is strong, and harmful gas can't be dissolved in water or the solubility is too low. The whole purifying chamber 9 is of a hollow structure.
The foregoing shows and describes the general principles, essential features, and advantages of the utility model. It will be understood by those skilled in the art that the present invention is not limited to the embodiments described above, which are intended to illustrate the principles of the utility model, but that various changes and modifications may be made without departing from the spirit and scope of the utility model, and the utility model is to be limited to the embodiments described above.
Claims (5)
1. The utility model provides a sediment VOCs is airtight to be collected processing system is arranged to furfural, a serial communication port, sediment belt conveyor (3) have been arranged to the below of cyclone (2), sediment belt conveyor (3) can move away the solid sediment that separates, mixed air inlet (1) have been arranged on cyclone (2), gas outlet (4) have been arranged to cyclone (2) top, second grade clean system (5) are being connected in gas outlet (4), trachea (6) once more are being connected in second grade clean system (5) through the pipeline, trachea (6) once more lead to whole clean room (9) that deposit room (7) and subside isolation room (10) constitute jointly, contain the partition wall between subside room (7) and the subside isolation room (10), it connects VOCS gas treatment connecting pipe (11) to stretch out the pipeline on subside isolation room (10).
2. The closed collection and treatment system for the furfural residues-discharged VOCs according to claim 1, wherein a filtering device is arranged inside the secondary purification system (5).
3. The closed collection and treatment system for the furfural residue-discharging VOCs according to claim 1, wherein a spray purification device is arranged inside the secondary purification system (5).
4. The closed collection and treatment system for the furfural residues-discharging VOCs according to claim 1, wherein a bottom wastewater storage area (8) is arranged below the settling chamber (7), and the wastewater storage area (8) is connected with a dilute acid configuration device through a pipeline.
5. The closed collection and treatment system for the furfural residues-discharged VOCs according to claim 1, wherein a wastewater tank (12) is arranged at the right side of the integral purification chamber (9), and the wastewater tank (12) is connected with a sewage treatment area through a water pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122486196.8U CN215822683U (en) | 2021-10-15 | 2021-10-15 | Closed collecting and processing system for VOCs (volatile organic compounds) in furfural slag discharge process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122486196.8U CN215822683U (en) | 2021-10-15 | 2021-10-15 | Closed collecting and processing system for VOCs (volatile organic compounds) in furfural slag discharge process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN215822683U true CN215822683U (en) | 2022-02-15 |
Family
ID=80202644
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202122486196.8U Active CN215822683U (en) | 2021-10-15 | 2021-10-15 | Closed collecting and processing system for VOCs (volatile organic compounds) in furfural slag discharge process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN215822683U (en) |
-
2021
- 2021-10-15 CN CN202122486196.8U patent/CN215822683U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204079685U (en) | A kind for the treatment of unit of high salinity high-COD waste water | |
| CN106986490B (en) | Process and device for recycling and treating industrial production wastewater of carboxylic ester | |
| CN206886896U (en) | A kind of municipal wastewater processing unit | |
| CN107162307A (en) | A kind of sewage-treatment plant | |
| CN102336650B (en) | Stripping process and device for removing organic impurities in brufen sodium salt | |
| CN215822683U (en) | Closed collecting and processing system for VOCs (volatile organic compounds) in furfural slag discharge process | |
| CN104891716B (en) | A kind of industrial wastewater, exhaust treatment system | |
| CN102367187B (en) | Chlorinated hydrocarbon-polluted underground water blowing oxidation and tail gas treatment process | |
| CN101544410A (en) | Industrial wastewater vacuum distillation purifier | |
| CN109133465A (en) | A kind of Waste Heat Reuse vacuum membrane distillation zero discharge treatment device and method | |
| CN105688629B (en) | It purifies anaerobic fermentation gas and recycles the method and system of phosphate and carbon dioxide | |
| CN111848396B (en) | Synthetic system of isooctyl acrylate | |
| CN210481018U (en) | Automatic drainage device for chemical product circulating water purification | |
| CN207347248U (en) | A kind of high-concentration organic wastewater treatment device | |
| CN115040899B (en) | Continuous dewatering device of triethylamine in glyphosate production process | |
| CN107792949A (en) | Packaged type Household sewage processor | |
| CN212102269U (en) | Multi-section type reclaimed water recycling treatment equipment | |
| CN204816125U (en) | High temperature waste gas processing system of polyamide apparatus for producing | |
| CN213231891U (en) | Automatic deoiling device in pharmaceutical intermediate waste water MVR evaporation crystallization | |
| CN216336955U (en) | Integrated sewage treatment device | |
| CN215404066U (en) | Dust collector for gas recovery and purification device | |
| CN216890174U (en) | Sewage multiple-effect evaporation processing system | |
| CN215756943U (en) | Industrial high-concentration wastewater treatment device | |
| CN212440585U (en) | Novel high-efficient dust shaker of fermentation | |
| CN216604060U (en) | Device for prolonging operation cycle of DMF evaporator |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20221209 Address after: 457000 intersection of Keji road and Xinghu Road, chemical industry cluster, Puyang City, Henan Province Patentee after: Henan Haosen biomaterials Co.,Ltd. Patentee after: SHANDONG YINO BIOLOGIC MATERIALS CO.,LTD. Address before: 457000 intersection of Keji road and Xinghu Road, chemical industry cluster, Puyang City, Henan Province Patentee before: Henan Haosen biomaterials Co.,Ltd. |
|
| TR01 | Transfer of patent right |