CN200963586Y - Chemical industry waste material regenerating device - Google Patents
Chemical industry waste material regenerating device Download PDFInfo
- Publication number
- CN200963586Y CN200963586Y CN 200620126742 CN200620126742U CN200963586Y CN 200963586 Y CN200963586 Y CN 200963586Y CN 200620126742 CN200620126742 CN 200620126742 CN 200620126742 U CN200620126742 U CN 200620126742U CN 200963586 Y CN200963586 Y CN 200963586Y
- Authority
- CN
- China
- Prior art keywords
- reactor
- chamber
- discharging
- reaction vessel
- material discharging
- 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
Images
Landscapes
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The utility model relates to a recycling device for chemical industry waste material, which comprises a reaction vessel, a heating device is arranged on the four walls of the reaction vessel, a material charging hole is arranged on the upper cover of the reaction vessel, a distilling tube is connected upwards with the middle of the upper cover, the distilling tube is communicated with a condensing chamber outwards, a condenser is arranged at the middle of the distilling tube, a material discharging hole is arranged at the bottom of the reaction vessel, the material discharging hole is connected with a degassing chamber of material discharging through a pipe, an exhaust pipe is arranged at the upside of the degassing chamber of material discharging, the exhaust pipe is connected with a tail gas treatment device; the utility model is also provided with a chamber for material preheating and melting and a device for material handling and charging. An electric heating device are packed outside a material discharging pipeline; a pipeline between the material discharging hole of the reaction vessel and the degassing chamber of material discharging is connected with a settling vessel. The utility model can recycle the waste material and slag from chemical industry, most of raw materials from the waste material and slag can be recovered by way of the reaction in the reaction vessel, a supplementary material and additive is added into the byproduct from the reaction, the cooled and condensed resin can be used as a raw material in paint material, rubber, printing ink adhesive and so forth; the recycling process does not produce slag in which the environment is protected, the pollution problem can be completely solved.
Description
Technical field
The utility model relates to a kind of waste recovery and utilizes equipment, particularly a kind of chemical spent material regenerating unit.
Background technology
Produce leftover bits and pieces waste residues such as benzylideneacetone, glutaraldehyde, cinnamic acid in the prior art, what have handles with the method for burning, and can produce a large amount of pernicious gases, contaminated environment; What have can only adopt buried method, but they can't degrade again, thoroughly the contaminated solution problem.And can be recycled in these waste residues, they are burned bury so in vain, too unfortunate.
Summary of the invention
The technical problems to be solved in the utility model is at the deficiencies in the prior art, has proposed a kind of chemical spent material regenerating unit of simple structure.
The technical problems to be solved in the utility model is achieved through the following technical solutions, a kind of chemical spent material regenerating unit, be characterized in: it is provided with a reactor, the wall of reactor is provided with heater, reactor is provided with a loam cake, on cover and be provided with charge door, middle part at loam cake upwards is connected with distillation cascade, distillation cascade outwards communicates with condensing chamber, middle part at distillation cascade is provided with condenser, is provided with discharging opening in the bottom of reactor, and discharging opening joins by pipeline and discharging deaerating chamber, the top of discharging deaerating chamber is provided with blast pipe, and blast pipe is connected with exhaust gas processing device.
The technical problems to be solved in the utility model can also come by the following technical programs further to realize that it also is provided with the material preheating and melts the chamber, melts in the material preheating to be provided with material transhipment delivery device between chamber and the reactor.
The technical problems to be solved in the utility model can also come to realize that further the pipeline between the discharging opening of reactor and the discharging deaerating chamber is coated with electric heater unit by the following technical programs.
The technical problems to be solved in the utility model can also come to realize that further be connected with the sedimentation still on the pipeline between the discharging opening of reactor and the discharging deaerating chamber, the wall of sedimentation still is provided with heating apparatus, is provided with agitator in the sedimentation still by the following technical programs.
The technical problems to be solved in the utility model can also be come by the following technical programs further to realize, be covered on the reactor blowout prevention Pot devices is housed.
Utilize the utility model device to producing leftover bits and pieces waste residues such as benzylideneacetone, glutaraldehyde, cinnamic acid, the processing of regenerating, through the reaction in the reactor, reclaim most of benzylideneacetone, glutaraldehyde, cinnamic acid raw material, its byproduct adds certain attached material and auxiliary agent in addition, and the resin of cooled and solidified can be used as the raw material of coating, rubber, ink binder etc.It is simple in structure, and treatment effect is good, and above-mentioned chemical spent material is disposed completely, has not a particle of waste residue.This device can not produce pernicious gas, has protected environment, has thoroughly solved pollution problem.
Description of drawings
Accompanying drawing is a structure diagram of the present utility model.
The specific embodiment
A kind of chemical spent material regenerating unit, it is provided with a reactor 3, and the wall of reactor 3 is provided with heater 4, reactor 3 is provided with a loam cake, on cover and be provided with charge door 5, charge door 5 places are provided with filter, remove the impurity foreign material, cover on the reactor 3 blowout prevention Pot devices 7 is housed.Middle part at loam cake upwards is connected with distillation cascade 6, distillation cascade 6 outwards communicates with condensing chamber 9, be provided with condenser 8 at the middle part of distillation cascade 6, be provided with discharging opening 14 in the bottom of reactor 3, discharging opening 14 joins by pipeline and discharging deaerating chamber 12, the top of discharging deaerating chamber 12 is provided with blast pipe 11, and blast pipe 11 is connected with exhaust gas processing device 10.It also is provided with the material preheating and melts chamber 1, melts in the material preheating to be provided with material transhipment delivery device 2 between chamber 1 and the reactor 3.Described heater 4 adopts conduction oil, heats by heat-conducting oil furnace.
Chemical spent material as: produce benzylideneacetone; glutaraldehyde; leftover bits and pieces waste residues such as cinnamic acid; at first chemical spent material is classified; pack into and transport bucket; send into material preheating thawing chamber 1 and preheat thawing; coarse filtration; through transhipment delivery device 2; liquid material in the transhipment bucket is dropped in the reactor 3; add certain attached material and auxiliary agent, the reaction gas in the reactor 3 leads in the condensing chamber 9 by distillation cascade 6 and is condensed into finished product, and the liquid in the reactor 3 is disposed to discharging deaerating chamber 12; the treated device of tail gas is handled the back discharging; reach state environmental emissioning standard, the protection environment, the resin of cooled and solidified can be used as coating; rubber; the raw material of ink binder etc.
The discharging opening 14 of reactor 3 and the pipeline between the discharging deaerating chamber 12 are coated with electric heater unit.Temperature is very high in the reactor 3, can not directly be discharged in the discharging degasification, need through after being cooled to uniform temperature, discharging again is after temperature is reduced to a certain degree, material can condense, so will on the discharging pipeline, install the electrical heating heating device additional, can on the discharging opening 14 of reactor 3 and the pipeline between the discharging deaerating chamber 12, install sedimentation still 15 additional, the wall of sedimentation still 15 is provided with heating apparatus 16, be provided with agitator 13 in the sedimentation still 15, sedimentation still 15 bottoms are provided with slag cleaning device.Material in the reactor 3 can be put into expansion chamber 15 earlier, cools off one by one, also will guarantee certain temperature in the expansion chamber 15, and it is excessive to prevent to lower the temperature.
Claims (5)
1. chemical spent material regenerating unit, it is characterized in that: it is provided with a reactor (3), the wall of reactor (3) is provided with heater (4), reactor (3) is provided with a loam cake, on cover and be provided with charge door (5), upwards be connected with distillation cascade (6) at the middle part of loam cake, distillation cascade (6) outwards communicates with condensing chamber (9), be provided with condenser (8) at the middle part of distillation cascade (6), be provided with discharging opening (14) in the bottom of reactor (3), discharging opening (14) joins by pipeline and discharging deaerating chamber (12), and the top of discharging deaerating chamber (12) is provided with blast pipe (11), and blast pipe (11) is connected with exhaust gas processing device (10).
2. chemical spent material regenerating unit according to claim 1 is characterized in that: it is provided with the material preheating and melts chamber (1), melts in the material preheating to be provided with material transhipment delivery device (2) between chamber (1) and the reactor (3).
3. chemical spent material regenerating unit according to claim 1 is characterized in that: the discharging opening (14) of reactor (3) and the pipeline between the discharging deaerating chamber (12) are coated with electric heater unit.
4. chemical spent material regenerating unit according to claim 1, it is characterized in that: be connected with sedimentation still (15) on the discharging opening (14) of reactor (3) and the pipeline between the discharging deaerating chamber (12), the wall of sedimentation still (15) is provided with heating apparatus (16), is provided with agitator (13) in the sedimentation still (15).
5. chemical spent material regenerating unit according to claim 1 is characterized in that: cover on the reactor (3) blowout prevention Pot devices (7) is housed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620126742 CN200963586Y (en) | 2006-11-01 | 2006-11-01 | Chemical industry waste material regenerating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620126742 CN200963586Y (en) | 2006-11-01 | 2006-11-01 | Chemical industry waste material regenerating device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN200963586Y true CN200963586Y (en) | 2007-10-24 |
Family
ID=38867601
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200620126742 Expired - Fee Related CN200963586Y (en) | 2006-11-01 | 2006-11-01 | Chemical industry waste material regenerating device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN200963586Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102274670A (en) * | 2010-06-10 | 2011-12-14 | 许培圣 | Trapping device adopted in resin synthesis |
| CN109319864A (en) * | 2018-10-31 | 2019-02-12 | 夏文峰 | A kind of system of energy saving and environment friendly recycling ink material |
| CN111643956A (en) * | 2020-05-27 | 2020-09-11 | 河北诚昊化工有限公司 | Device for purifying and saving raw materials by discharging pollution discharged from distillation kettle into buffer tank |
-
2006
- 2006-11-01 CN CN 200620126742 patent/CN200963586Y/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102274670A (en) * | 2010-06-10 | 2011-12-14 | 许培圣 | Trapping device adopted in resin synthesis |
| CN102274670B (en) * | 2010-06-10 | 2013-08-28 | 许培圣 | Trapping device adopted in resin synthesis |
| CN109319864A (en) * | 2018-10-31 | 2019-02-12 | 夏文峰 | A kind of system of energy saving and environment friendly recycling ink material |
| CN109319864B (en) * | 2018-10-31 | 2021-04-30 | 安徽永桦包装有限公司 | Energy-saving and environment-friendly system for recovering printing ink materials |
| CN111643956A (en) * | 2020-05-27 | 2020-09-11 | 河北诚昊化工有限公司 | Device for purifying and saving raw materials by discharging pollution discharged from distillation kettle into buffer tank |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US5632863A (en) | Battery pyrolysis process | |
| CN102164996B (en) | Process and apparatus for decomposition of polymer products including those containing sulphur such as vulcanised rubber tyres and recovery of resources therefrom | |
| CN207787253U (en) | A kind of system of old circuit board Pyrolyzation and debromination processing | |
| CN100494430C (en) | Method for producing zinc alloy from zinc dross | |
| US10808294B2 (en) | Triple chamber furnace for scrap segregation and melting | |
| CN107891053A (en) | A kind of method and system of old circuit board Pyrolyzation and debromination processing | |
| CN200963586Y (en) | Chemical industry waste material regenerating device | |
| JPH09287033A (en) | Treatment of waste containing oxide and method therefor | |
| CN1207410C (en) | Magnesium alloy waste regenerator | |
| TW200537169A (en) | Use of liquid-crystal displays, and processes for the recycling thereof | |
| CN104694759A (en) | Recycling method of metal-containing powder in waste printed circuit board | |
| JPH0789900A (en) | Method for recovering high-quality monomer from plastic | |
| CN1043251C (en) | Method and apparatus of treating dusts containing oxides | |
| JP3959009B2 (en) | Thermal decomposition recycling method of organic matter | |
| CN108787695A (en) | A method of stereotype grid and plastics in the broken rear lead-acid accumulator of separation | |
| JP3346300B2 (en) | Method for recovering polymer components from waste plastic | |
| WO1999021619A1 (en) | Method for treating household refuse incinerator ash | |
| JP4445177B2 (en) | Method using gas from settling tank | |
| CA2776574A1 (en) | Method and reactor for processing bulk material containing li | |
| JPS6160840A (en) | Processing method of refuse containing mercury | |
| JP2001239231A (en) | Method of recovering heavy metals from discharged material in waste incineration facility | |
| JP3745996B2 (en) | Processing method of aluminum ash | |
| CN102041391A (en) | Method for separating and extracting pure aluminium from material containing metallic aluminium | |
| JP3759559B2 (en) | Heat medium for treating polymer-containing waste and method for treating polymer-containing waste | |
| CN219995336U (en) | Waste circuit board pyrolysis melting test device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20071024 Termination date: 20101101 |