CN204058312U - The device of furfural is extracted from paper waste - Google Patents
The device of furfural is extracted from paper waste Download PDFInfo
- Publication number
- CN204058312U CN204058312U CN201420468135.6U CN201420468135U CN204058312U CN 204058312 U CN204058312 U CN 204058312U CN 201420468135 U CN201420468135 U CN 201420468135U CN 204058312 U CN204058312 U CN 204058312U
- Authority
- CN
- China
- Prior art keywords
- tower
- furfural
- primary
- reaction pot
- dehydration
- 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.)
- Withdrawn - After Issue
Links
Landscapes
- Paper (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The device of furfural is extracted from paper waste, primarily of primary tower, dehydration tower and treating tower composition, before primary tower, pretreatment unit is set, pretreatment unit comprises removal of impurities tower, thickener, hydrolytic reaction pot and original fluid container, the tower reactor of removal of impurities tower is connected with thickener, thickener is connected with hydrolytic reaction pot, hydrolytic reaction pot top is connected with original fluid container by condenser, original fluid container is connected in the middle part of primary tower by pipeline, primary tower overhead condenser is connected with a phase splitter, phase splitter is connected with dehydration tower with primary tower respectively, dehydration tower tower reactor is connected with treating tower by pipeline.The utility model by arranging pretreatment unit before primary tower, to be unfavorable in paper waste that xylose is the material removing of furfural, thus by the xylose furfural in papermaking wastewater, both can extract the furfural product that economic worth is high, and wastewater treatment expense can have been reduced again.
Description
Technical field
The utility model relates to furfural production and pulping wastewater treatment technical field, is specifically related to a kind of device extracting furfural from paper waste.
Background technology
Paper industry producer of current China, the waste liquid major part of new generation does not make full use of, especially be the paper mill of raw material with timber, it is higher that it discharges waste liquid Xylose Content, be approximately 5 ~ 8%, its waste liquid is bad process also, serious environment pollution, processing costs is invested higher when processing, for Shandong Sun Paper Group, produce waste water about more than 1,600 ton every day, wherein Xylose Content is 5 ~ 8%, as being processed into furfural, 56 tons, furfural can be obtained every day, 18480 tons, furfural can be produced every year, by price per ton 0.9 ten thousand yuan, 1.66 hundred million yuan can be increased income every year, the waste water ratio extracted after furfural better processes, save wastewater treatment expense.
Summary of the invention
The utility model provides a kind of device extracting furfural from paper waste, to solve the problem of the bad process contaminate environment of paper waste that prior art exists.
The utility model device is primarily of primary tower, dehydration tower and treating tower composition, solving the technical scheme that its technical problem adopts is arrange pretreatment unit before primary tower, pretreatment unit comprises removal of impurities tower, thickener, hydrolytic reaction pot and original fluid container, the tower reactor of removal of impurities tower is connected with thickener, thickener is connected with hydrolytic reaction pot, hydrolytic reaction pot top is connected with original fluid container by condenser, original fluid container is connected in the middle part of primary tower by pipeline, primary tower overhead condenser is connected with a phase splitter, phase splitter is connected with dehydration tower with primary tower respectively, dehydration tower tower reactor is connected with treating tower by pipeline.
Above-mentioned phase splitter be connected a neutralization tank between dehydration tower.
Principle of work of the present utility model is: paper waste is carried out pre-treatment, to be unfavorable in paper waste that xylose is the material removing of furfural, the paper waste of removing impurity carry out concentrated after deliver to acid adding in hydrolytic reaction pot, wherein wood sugar of heating is sloughed three water and is converted into furfural, draw furfural steam through the laggard primary tower distillation of condenser condenses, layering in phase splitter is gone in overhead vapours condensation 40 DEG C, water aldehyde returns primary tower, aldehyde layer adds in alkali and rear dehydration, refining generation finished product furfural, concrete technology step is as follows:
(1) paper waste is got in removal of impurity tower, remove methyl alcohol, acetone and light constituent that unfavorable xylose in waste water is furfural;
(2) make to send into hydrolytic reaction pot after wood sugar mass concentration reaches 16.92% in waste liquid by carrying out concentrating in the paper waste after the removal of impurity early thickener;
(3) waste water after concentrated is squeezed into hydrolytic reaction pot and add acetic acid simultaneously, acetic acid consumption is 4.5% of wastewater quality;
(4) open steam and carry out increasing temperature and pressure to the waste water of hydrolytic reaction pot, control temperature of reaction at 180 DEG C, controlling the reaction times is 375 minutes;
(5) when material reaction in hydrolytic reaction pot is after 1 hour, open out aldehyde valve, drawn by aldehyde steam and obtain stoste through condensing cooling, hydrolytic reaction pot keeps 180 DEG C;
(6) stoste is entered after primary tower distills, and steam send phase-splitting in phase splitter through condenser condenses to 40 DEG C;
(7) water aldehyde passes back into tower, aldehyde enter mutually in neutralization tank through to add in alkali and after send dehydration tower to dewater;
(8) aldehyde that dewaters send treating column to carry out refining obtaining finished product furfural.
The utility model by arranging pretreatment unit before primary tower, to be unfavorable in paper waste that xylose is the material removing of furfural, thus by the xylose furfural in papermaking wastewater, (in waste water, Xylose Content is 7% to each 1,600 tons of waste water, furfural 5% can be carried) 56 tons of furfurals can be extracted, calculated by 1 year and can extract 18480 tons, furfural, by 0.9 ten thousand yuan of calculating per ton, can increase income into 1.66 hundred million yuan every year, the waste water of new generation can extract acetic acid or produce sodium-acetate administers waste water again, reduces wastewater treatment expense.
Accompanying drawing explanation
Below in conjunction with drawings and Examples, the utility model is further illustrated.
Fig. 1 is the structural representation of the utility model device.
1 removal of impurities tower, 2 thickeners, 3 hydrolytic reaction pots, 4 condensers, 5 original fluid containers, 6 primary towers, 7 phase splitters, 8 neutralization tanks, 9 dehydration towers, 10 treating towers in figure.
Embodiment
As shown in the figure, a kind of device extracting furfural from paper waste, primarily of primary tower 6, dehydration tower 9 and treating tower 10 form, before primary tower 6, pretreatment unit is set, pretreatment unit comprises removal of impurities tower 1, thickener 2, hydrolytic reaction pot 3 and original fluid container 5, the tower reactor of removal of impurities tower 1 is connected with thickener 2, thickener 2 is connected with hydrolytic reaction pot 3, hydrolytic reaction pot 3 top is connected with original fluid container 5 by condenser 4, original fluid container 5 is connected in the middle part of primary tower 6 by pipeline, primary tower 6 overhead condenser is connected with a phase splitter 7, phase splitter 7 is connected with dehydration tower 9 with primary tower 6 respectively, a neutralization tank 8 is connected between phase splitter 7 with dehydration tower 9, dehydration tower 9 tower reactor is connected with treating tower 10 by pipeline.
The technique extracting furfural from paper waste of the present utility model is: extract from paper waste in the device of furfural above-mentioned, paper waste is carried out pre-treatment, to be unfavorable in paper waste that xylose is the material removing of furfural, the paper waste of removing impurity carry out concentrated after deliver to acid adding in hydrolytic reaction pot, wherein wood sugar of heating is sloughed three water and is converted into furfural, draw furfural steam through the laggard primary tower distillation of condenser condenses, layering in phase splitter is gone in overhead vapours condensation 40 DEG C, water aldehyde returns primary tower, aldehyde layer adds in alkali and rear dehydration, refining generation finished product furfural, concrete technology step is as follows:
(1) paper waste is got in removal of impurity tower 1, remove methyl alcohol, acetone and light constituent that unfavorable xylose in waste water is furfural;
(2) paper waste after the removal of impurity is carried out in thickener 2 concentrated make wood sugar mass concentration in waste liquid reach 16.92% after send into hydrolytic reaction pot 3;
(3) waste water after concentrated is squeezed into hydrolytic reaction pot 3 and add acetic acid simultaneously, acetic acid consumption is 4.5% of wastewater quality;
(4) open steam and carry out increasing temperature and pressure to the waste water of hydrolytic reaction pot 3, control temperature of reaction at 180 DEG C, controlling the reaction times is 375 minutes;
(5) when material reaction in hydrolytic reaction pot 3 is after 1 hour, open out aldehyde valve, drawn by aldehyde steam and obtain stoste through condensing cooling, hydrolytic reaction pot 3 keeps 180 DEG C;
(6) stoste is entered after primary tower 6 distills, and steam send phase-splitting in phase splitter 7 through condenser condenses to 40 DEG C;
(7) water aldehyde passes back into tower, aldehyde enter mutually in neutralization tank 8 through to add in alkali and after send dehydration tower 9 to dewater;
Dehydration aldehyde send treating column 10 to refine, and obtains finished product furfural from tower top.
Claims (2)
1. one kind is extracted the device of furfural from paper waste, primarily of primary tower, dehydration tower and treating tower composition, it is characterized in that arranging pretreatment unit before primary tower, pretreatment unit comprises removal of impurities tower, thickener, hydrolytic reaction pot and original fluid container, the tower reactor of removal of impurities tower is connected with thickener, thickener is connected with hydrolytic reaction pot, hydrolytic reaction pot top is connected with original fluid container by condenser, original fluid container is connected in the middle part of primary tower by pipeline, primary tower overhead condenser is connected with a phase splitter, phase splitter is connected with dehydration tower with primary tower respectively, dehydration tower tower reactor is connected with treating tower by pipeline.
2. the device extracting furfural from paper waste according to claim 1, is characterized in that being connected a neutralization tank between phase splitter with dehydration tower.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420468135.6U CN204058312U (en) | 2014-08-19 | 2014-08-19 | The device of furfural is extracted from paper waste |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420468135.6U CN204058312U (en) | 2014-08-19 | 2014-08-19 | The device of furfural is extracted from paper waste |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204058312U true CN204058312U (en) | 2014-12-31 |
Family
ID=52199864
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420468135.6U Withdrawn - After Issue CN204058312U (en) | 2014-08-19 | 2014-08-19 | The device of furfural is extracted from paper waste |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204058312U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104151273A (en) * | 2014-08-19 | 2014-11-19 | 衡水中科信能源有限公司 | Apparatus and technology for extracting furfural in papermaking waste water |
-
2014
- 2014-08-19 CN CN201420468135.6U patent/CN204058312U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104151273A (en) * | 2014-08-19 | 2014-11-19 | 衡水中科信能源有限公司 | Apparatus and technology for extracting furfural in papermaking waste water |
| CN104151273B (en) * | 2014-08-19 | 2016-01-06 | 衡水中科信能源有限公司 | Device and the technique of furfural is extracted from paper waste |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100453137C (en) | Alcohol quinque-towel differential pressure distilling arrangement and technique thereof | |
| CN100525874C (en) | Six-column differential-pressure distillation device for extra edible alcohol and process therefor | |
| CN102675265B (en) | Method of refining furfural through six-tower continuous rectification | |
| CN106928026B (en) | Method for distilling cellulosic ethanol | |
| CN202849381U (en) | Device for efficiently and comprehensively utilizing potato starch wastewater | |
| CN104130224A (en) | Six-tower type continuous refining device for furfural production and furfural refining process thereof | |
| CN102776074A (en) | Method for producing fatty acid from plant oil scraps | |
| CN103614278A (en) | Device and method for processing molasses alcohol waste liquor | |
| CN211170524U (en) | Preparation system of adipic acid dibasic ester | |
| CN104151273B (en) | Device and the technique of furfural is extracted from paper waste | |
| CN110698325A (en) | Production device and process for co-producing fuel ethanol and special grade edible alcohol | |
| CN202658123U (en) | High-efficiency, energy-saving, low-cost and high-quality rosin production line equipment | |
| CN204058312U (en) | The device of furfural is extracted from paper waste | |
| CN204897793U (en) | DOTP plasticizer esterification reaction device | |
| CN101475444B (en) | Partial dehydration and purification process for crude glycerine | |
| CN210419808U (en) | Fusel recovery system in BDO device waste liquid | |
| CN102924231B (en) | For producing the method and apparatus of the triple effect distillation of alcohol | |
| CN204051037U (en) | Furfural continuous rectification apparatus | |
| CN102827115A (en) | Continuous refining system for producing maleic anhydride | |
| CN202989109U (en) | Novel reboiling device | |
| CN107129103B (en) | Comprehensive treatment and utilization process and method for furfural production wastewater | |
| CN204918432U (en) | Ester class plasticizer serialization dealcoholize system | |
| CN205216249U (en) | Ethyl methyl ketone drying tower | |
| CN203602599U (en) | Equipment for processing molasses alcohol liquid waste | |
| CN204147853U (en) | A kind of reaction dewater unit |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20141231 Effective date of abandoning: 20160106 |
|
| C25 | Abandonment of patent right or utility model to avoid double patenting |