CN202390380U - Gasification device for saponin hydrolysate extraction residues - Google Patents
Gasification device for saponin hydrolysate extraction residues Download PDFInfo
- Publication number
- CN202390380U CN202390380U CN2011205098192U CN201120509819U CN202390380U CN 202390380 U CN202390380 U CN 202390380U CN 2011205098192 U CN2011205098192 U CN 2011205098192U CN 201120509819 U CN201120509819 U CN 201120509819U CN 202390380 U CN202390380 U CN 202390380U
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- CN
- China
- Prior art keywords
- gasification furnace
- dust precipitator
- vapourizing furnace
- gasification
- pipeline
- 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
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
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- Gasification And Melting Of Waste (AREA)
Abstract
The utility model provides a gasification device for saponin hydrolysate extraction residues, which comprises a gasification furnace. A spiral feeder is arranged at a feeding port of the gasification furnace; an ash outlet is arranged at the bottom of the gasification furnace, a primary dust precipitator is connected to the top or the lateral wall of the gasification furnace through a pipeline and then connected with a secondary dust precipitator through a pipeline, and an output pipeline is arranged at the top of the secondary dust precipitator; the primary dust precipitator and the secondary dust precipitator are provided with funnel-shaped ash outlets; a blasting unit is arranged at the bottom of the gasification furnace, and an observing port is arranged on the lateral wall at the bottom of the gasification furnace; a temperature sensor is arranged on the lateral wall of the gasification furnace; and a water tank is arranged at the ash outlet. When the gasification device is used, combustible gases in the gasification furnace are output through the primary dust precipitator and the secondary dust precipitator successively, and waste is successively discharged through the ash outlets at the bottom of the gasification furnace and in the primary dust precipitator and the secondary dust precipitator after multi-stage de-dusting, and transmitted into a boiler to serve as energy to be re-burnt and release thermal energy. The gasification device has the advantages of saving energy, creating benefits and protecting the environment.
Description
Technical field
The utility model relates to a kind of saponin hydrolysate extraction residue gasification installation.
Background technology
All the time, all face product per ton and have surplus in the of ten the residue treatment problem after the extraction of ton at the saponin production industry, a large amount of residues are heaped, and each major company also thought a lot of methods, and burying to fill out needs a large amount of human and material resources, more needs the landfill place; Burning causes very big smog and dust, because the long potential safety hazard that also stayed of powder burning time, the phenomenon of dying that takes place to burn happens occasionally.Be placed directly in the boiler and burn, boiler grate is caused very major injury and waste fire coal.
Summary of the invention
The utility model is in order to let the residue of saponin hydrolysate make full use of and protect boiler, and the spy proposes a kind of saponin hydrolysate extraction residue gasification installation.
The technical scheme of the utility model does for this reason, and saponin hydrolysate extraction residue gasification installation comprises a vapourizing furnace, it is characterized in that: the opening for feed place at vapourizing furnace is provided with feeding screw; The bottom of vapourizing furnace is provided with ash output hole, and the top or the sidewall of vapourizing furnace are connected with disposable dust remover through pipeline, and disposable dust remover is connected with secondary filter again through pipeline, and the top of secondary filter is provided with delivery conduit; Wherein disposable dust remover and secondary filter are provided with the funnel-form ash output hole.
Improvement to such scheme is: the bottom at vapourizing furnace is provided with air-blast device, and the sidewall of vapourizing furnace bottom is provided with porthole.
Improvement to such scheme is: on the sidewall of vapourizing furnace, be provided with TP.
Improvement to such scheme is: the place is provided with water tank at ash output hole.
Beneficial effect:
The utility model is in use exported the inflammable gas in the vapourizing furnace successively through disposable dust remover and secondary filter; And get rid of waste material at the discharge port of the bottom of vapourizing furnace and disposable dust remover and secondary filter successively; The gasification technology that utilizes is under thermodynamic condition, lets its burning under the situation of few oxygen produce carbon monoxide (CO), hydrogen (H
2), methane (CH
4) blended burning gas body, let this gas discharge its heat energy as energy reignition through being delivered into boiler after the multistage dedusting.
The hydrolyzate residue of combustion matter heat 2500 kilocalories is at the uniform velocity sent in the vapourizing furnace through spiral custody transfer machine, let it produce combustible CO, H
2, CH
4Mixed gas, utilize pressure that oxygen supply incendiary gas blower produces that gas is delivered to the furnace roof of combustion chamber, via twice cyclone dust removal apparatus, the height combustion matter Purge gas after twice dedusting is being sent into boiler combustion through transport pipe.
Design a plurality of ash output holes, and ash output hole has water tank to connect to avoid full of smoke, the gas cleaning is dustless, no tar.Feeding screw is adopted in charging; Reduced potential safety hazard; For guaranteeing company's inertia of charging and air feed; TP is set on body of heater, and operator show the optimum regime of controlling and regulating stove internal combustion district and producing flammable gas area according to thermometer, to keep the continuity that at the uniform velocity charging guarantees air feed.
Because the calorific value of hydrolyzate residue is approximately 2500 kilocalories; Not only solve the heap problem of residue, turn waste into wealth especially, become the novel energy of sustainable use; The energy that utilizes gasification to produce is used for producing, heating not only solves environmental pollution but also can bring benefits; Compare other vapourizing furnace, not only captured dust, the tar of gasification, last residue can be made gac.
Having practiced thrift the energy has created benefit and has protected environment.
Description of drawings
Fig. 1 is the structural representation of the utility model.
1 is vapourizing furnace among the figure, the 2nd, and feeding screw, the 3rd, porthole, the 4th, ash output hole, the 5th, air-blast device,
The 6th, disposable dust remover, the 7th, secondary filter, the 8th, pipeline, the 9th, delivery conduit, the 10th, TP, the 11st, water tank.
Embodiment
The utility model saponin hydrolysate extraction residue gasification installation as shown in Figure 1ly comprises a vapourizing furnace 1, is provided with feeding screw 2 at the opening for feed place of vapourizing furnace 1; The bottom of vapourizing furnace 1 is provided with ash output hole 4, and the top of vapourizing furnace 1 or sidewall are connected with disposable dust remover 6 through pipeline 8, and disposable dust remover 6 is connected with secondary filter 7 again through pipeline 8, and the top of secondary filter 7 is provided with delivery conduit 9; Wherein disposable dust remover 6 is provided with the funnel-form ash output hole with secondary filter 7.
Be provided with air-blast device 5 in the bottom of vapourizing furnace 1, the sidewall of vapourizing furnace 1 bottom is provided with porthole 3.
On the sidewall of vapourizing furnace 1, be provided with TP 10.
Funnel-form ash output hole at ash output hole 4 places and disposable dust remover 6 and secondary filter 7 is provided with water tank 11.
Claims (4)
1. saponin hydrolysate extraction residue gasification installation comprises a vapourizing furnace, it is characterized in that: the opening for feed place at vapourizing furnace is provided with feeding screw; The bottom of vapourizing furnace is provided with ash output hole, and the top or the sidewall of vapourizing furnace are connected with disposable dust remover through pipeline, and disposable dust remover is connected with secondary filter again through pipeline, and the top of secondary filter is provided with delivery conduit; Wherein disposable dust remover and secondary filter are provided with the funnel-form ash output hole.
2. saponin hydrolysate extraction residue gasification installation according to claim 1, it is characterized in that: the bottom at vapourizing furnace is provided with air-blast device, and the sidewall of vapourizing furnace bottom is provided with porthole.
3. saponin hydrolysate extraction residue gasification installation according to claim 1 and 2 is characterized in that: on the sidewall of vapourizing furnace, be provided with TP.
4. saponin hydrolysate extraction residue gasification installation according to claim 1, it is characterized in that: the place is provided with water tank at ash output hole.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011205098192U CN202390380U (en) | 2011-12-09 | 2011-12-09 | Gasification device for saponin hydrolysate extraction residues |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011205098192U CN202390380U (en) | 2011-12-09 | 2011-12-09 | Gasification device for saponin hydrolysate extraction residues |
Publications (1)
Publication Number | Publication Date |
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CN202390380U true CN202390380U (en) | 2012-08-22 |
Family
ID=46665318
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2011205098192U Expired - Fee Related CN202390380U (en) | 2011-12-09 | 2011-12-09 | Gasification device for saponin hydrolysate extraction residues |
Country Status (1)
Country | Link |
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CN (1) | CN202390380U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102517076A (en) * | 2011-12-09 | 2012-06-27 | 竹溪县康辉生物化工有限责任公司 | Gasification equipment of saponin hydrolysates extraction residue |
-
2011
- 2011-12-09 CN CN2011205098192U patent/CN202390380U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102517076A (en) * | 2011-12-09 | 2012-06-27 | 竹溪县康辉生物化工有限责任公司 | Gasification equipment of saponin hydrolysates extraction residue |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120822 Termination date: 20161209 |
|
CF01 | Termination of patent right due to non-payment of annual fee |