CN206896865U - Distilling apparatus - Google Patents
Distilling apparatus Download PDFInfo
- Publication number
- CN206896865U CN206896865U CN201720450650.5U CN201720450650U CN206896865U CN 206896865 U CN206896865 U CN 206896865U CN 201720450650 U CN201720450650 U CN 201720450650U CN 206896865 U CN206896865 U CN 206896865U
- Authority
- CN
- China
- Prior art keywords
- condenser
- reaction unit
- cooling pond
- distilling apparatus
- utility
- 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
Abstract
Rosin processing technique field is the utility model is related to, specifically a kind of distilling apparatus.Including reaction unit, condenser and cooling pond, the reaction unit top is provided with efferent duct, the reaction unit is connected by efferent duct with the condenser, the condenser lower end is provided with cooling pond, the cooling pond is connected by a connecting tube with the condenser, feed tube and drain pipe are not provided with above the condenser, and the water side of the drain pipe is provided with clarifier-tank.The utility model has the advantages of eliminating pernicious gas, resource recycling and low production cost caused by processing.
Description
Technical field
Rosin processing technique field is the utility model is related to, specifically a kind of distilling apparatus.
Background technology
Rosin is the non-volatile natural resin that is obtained by different processing modes using pine resin as raw material.Rosin
It is important industrial chemicals, is widely used in the industries such as soap, papermaking, paint, rubber.
In the process of rosin, existing process equipment often endangers work people in the presence of generation pernicious gas when processing
The health of member, meanwhile, in current softening agent production, because of the shortage of its raw material, rising violently for its price is caused, therefore,
It is badly in need of a kind of processing method for the softening agent that production cost is low and resource recycling rate is big.
Utility model content
For above-mentioned weak point of the prior art, the utility model aims to provide a kind of eliminate to be had caused by processing
Evil gas, resource recycling and the low distilling apparatus of production cost.
In order to solve the above technical problems, distilling apparatus of the present utility model, including reaction unit, condenser and cooling water
Pond, the reaction unit top are provided with efferent duct, and the reaction unit is connected by efferent duct with the condenser, described cold
Condenser lower end is provided with cooling pond, and the cooling pond is connected by a connecting tube with the condenser, on the condenser
Side is not provided with feed tube and drain pipe, and the water side of the drain pipe is provided with clarifier-tank.
Preferably, the reaction unit is arranged at including import, outlet and an at least Oil Guide heat-generating pipe, the import
The lower end of the reaction unit, described export are arranged at the upper end of the reaction unit, the Oil Guide heat-generating pipe level through
In whole reaction unit.
Preferably, the quantity of the Oil Guide heat-generating pipe is 7.
Preferably, the entrance point of the feed tube is connected with the cooling pond, and the port of export is connected with the condenser.
Distilling apparatus of the present utility model has advantages below：1st, the present apparatus has to handle during processing and produced in solid waste
Pernicious gas so that staff in work softening agent will not because solid waste heat caused by pernicious gas to body
Infringement, ensure that the health and safety of staff.2nd, using present apparatus work softening agent, because its raw material uses solid waste,
Therefore, its cost is low, at the same can also Resource recovery, reach the purposes of energy-conserving and environment-protective, meet the standard of green production.3rd, this dress
Put low with production cost, resource utilization is big and waste material produces the advantages of small.
Brief description of the drawings
Fig. 1 is the structural representation of distilling apparatus of the present utility model.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the embodiment of the utility model is carried out
Clearly and completely describe.
As shown in figure 1, distilling apparatus of the present utility model, including reaction unit 1, condenser 2 and cooling pond 3, it is described
The top of reaction unit 1 is provided with efferent duct 4, and the reaction unit 1 is connected by efferent duct 4 with the condenser 2, the condensation
The lower end of device 2 is provided with cooling pond 3, and the cooling pond 3 is connected by a connecting tube 5 with the condenser 2, the condenser
2 tops are not provided with feed tube 6 and drain pipe 7, and the water side of the drain pipe 7 is provided with clarifier-tank 8.
Further, the reaction unit 1 includes import 11, outlet 12 and an at least Oil Guide heat-generating pipe 13, it is described enter
Mouth 11 is arranged at the lower end of the reaction unit 1, and the outlet 12 is arranged at the upper ends of the reaction unit 1, the Oil Guide hair
Heat pipe 13 is horizontal through in whole reaction unit 1.
Further, the quantity of the Oil Guide heat-generating pipe 13 is 7.
Further, the entrance point of the feed tube 6 is connected with the cooling pond 3, the port of export and the condenser 2
Connection.
Specifically, being crushed solid waste for the first time using reducing mechanism during use, solid particle is obtained after crushing, then
Solid particle is put into carrier conduction oil, progress first time distillation in reaction unit 1 is imported into through import 11, by temperature control
System removes moisture removal between 300~320 DEG C；The material after moisture removal will be gone to be imported into by efferent duct 4 in condenser 2, condensed
Material is condensed into enter in cooling pond 3 after liquid and cooled down by device 2, filter off removing by clarifier-tank 8 after cooling
Impurity, reuse pulverizer and carry out separating twice, be then placed again into carrier conduction oil, reaction is imported into through import 11
Second distillation is carried out in device 1, by temperature control between 280~300 DEG C, softening agent is produced after second distillation.
Obviously, described embodiment is only part of the embodiment of the present utility model, rather than whole embodiments.
Based on the embodiment in the utility model, what those of ordinary skill in the art were obtained under the premise of creative work is not made
All other embodiment, belong to the scope of the utility model protection.
Claims (4)
1. a kind of distilling apparatus, including reaction unit (1), condenser (2) and cooling pond (3), it is characterised in that：The reaction
Device (1) top is provided with efferent duct (4), and the reaction unit (1) is connected by efferent duct (4) with the condenser (2), institute
State condenser (2) lower end and be provided with cooling pond (3), the cooling pond (3) passes through a connecting tube (5) and the condenser
(2) connect, be not provided with feed tube (6) and drain pipe (7) above the condenser (2), the water side of the drain pipe (7) is set
It is equipped with clarifier-tank (8).
2. distilling apparatus according to claim 1, it is characterised in that：The reaction unit (1) includes import (11), outlet
(12) and an at least Oil Guide heat-generating pipe (13), the import (11) is arranged at the lower end of the reaction unit (1), it is described go out
Mouth (12) is arranged at the upper end of the reaction unit (1), and the Oil Guide heat-generating pipe (13) is horizontal through whole reaction unit (1)
It is interior.
3. distilling apparatus according to claim 2, it is characterised in that：The quantity of the Oil Guide heat-generating pipe (13) is 7.
4. distilling apparatus according to claim 1, it is characterised in that：The entrance point of the feed tube (6) and the cooling
Pond (3) is connected, and the port of export is connected with the condenser (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720450650.5U CN206896865U (en) | 2017-04-26 | 2017-04-26 | Distilling apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720450650.5U CN206896865U (en) | 2017-04-26 | 2017-04-26 | Distilling apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206896865U true CN206896865U (en) | 2018-01-19 |
Family
ID=61291364
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720450650.5U Expired - Fee Related CN206896865U (en) | 2017-04-26 | 2017-04-26 | Distilling apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206896865U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106890473A (en) * | 2017-04-26 | 2017-06-27 | 贵州林亚达林化科技有限责任公司 | Distilling apparatus and the method using the device work softening agent |
-
2017
- 2017-04-26 CN CN201720450650.5U patent/CN206896865U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106890473A (en) * | 2017-04-26 | 2017-06-27 | 贵州林亚达林化科技有限责任公司 | Distilling apparatus and the method using the device work softening agent |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203916447U (en) | A kind of chlorosilane tail gas wet method wash mill | |
| CN204400885U (en) | The purification and recover equipment of solvent dimethyl sulfoxide (DMSO) in a kind of carbon fiber production process | |
| CN206896865U (en) | Distilling apparatus | |
| CN206089622U (en) | High accuracy flower bud of lily magnolia flower extraction of essential oil device | |
| CN103393159B (en) | High-yield environmentally-friendly fishmeal and fish oil production line equipment | |
| CN206011496U (en) | A kind of environmental protection high efficiency and energy-saving comminutor | |
| CN101658752A (en) | Recycling device of waste gas generated by producing rubber ingredients | |
| CN204848699U (en) | Acetylene is retrieved to carbide slag thick liquid and peace and quiet useless sodium hypochlorite uses multipurposely combined unit | |
| CN106629731A (en) | Method for recycling and processing waste silicon mud | |
| CN106890473A (en) | Distilling apparatus and the method using the device work softening agent | |
| CN207071314U (en) | A kind of acid mist treatment device of smoke test machine | |
| CN202808644U (en) | Device for continuously recovering acetylene from carbide slag slurry | |
| CN103961966B (en) | A kind of system that solves acid-restoring plant dynamic wave furnace gas temperature superelevation | |
| CN203874636U (en) | Adjustable vacuum protection device for treating tail gas generated by rosin resin production | |
| CN206746015U (en) | A kind of distilling apparatus of efficiently distilation recovery chlorobenzene | |
| CN207062041U (en) | The system for purifying waste acid | |
| CN203400518U (en) | Toluene recycling and rectifying device | |
| CN204224493U (en) | A kind of alcohol recovering device for alpha.-acetylacetanilide synthesis | |
| CN205867934U (en) | Continuous recovery unit of nitric acid tail gas | |
| CN204932941U (en) | A kind of pre-cold mould refrigerated separation structure | |
| CN202460204U (en) | Gas and liquid separator for esterification | |
| CN206214978U (en) | A kind of waste gas collection device of rosin resin production | |
| CN206823203U (en) | The condensing unit of external circulation evaporator | |
| CN103588734A (en) | Recovery method and recovery device of butyl ester and acetone in ketene dimer production | |
| CN203353615U (en) | High-yield environment friendly fish meal and fish oil production line 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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180119 |