CN201065384Y - Hydrolysis pot - Google Patents
Hydrolysis pot Download PDFInfo
- Publication number
- CN201065384Y CN201065384Y CNU2007201067998U CN200720106799U CN201065384Y CN 201065384 Y CN201065384 Y CN 201065384Y CN U2007201067998 U CNU2007201067998 U CN U2007201067998U CN 200720106799 U CN200720106799 U CN 200720106799U CN 201065384 Y CN201065384 Y CN 201065384Y
- Authority
- CN
- China
- Prior art keywords
- valve
- cylinder
- cylindrical shell
- tapered nozzle
- taper
- 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
Classifications
-
- 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
Landscapes
- Fertilizers (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The utility model relates to a garbage processing equipment, in particular to a hydrolysis equipment, which comprises a tubular cylinder; wherein, the cylinder is connected with an elliptical head at the upper part; a feeding opening is arranged at the central section of the elliptical head which is provided with a safety valve and an vent valve; a tapered nozzle is connected with the lower part of the cylinder; a discharging opening is arranged at the central section of the tapered nozzle and is provided with an outlet pneumatic valve, a steam valve and a drain valve; an air inlet valve is arranged at the connection part for the tapered nozzle and the cylinder; the air inlet valve is connected with an air duct which is coiled in the tapered nozzle. An observation port is arranged at the lateral face of the cylinder; both pressure gauge and thermometer are arranged for all the observation ports, the vent valve and the air inlet valve. The utility model has the advantages of successfully transplanting fermentation production technology in biological-pharmacy to organic manure composting fermentation production, greatly shortening production cycle, thoroughly, safely, hygienic and reliably fermenting and decomposition and having good dehydration result.
Description
Technical field
The utility model relates to a kind of refuse treatment plant, especially a kind of hydrolysis device.
Background technology
The municipal wastes problem has become one of the most serious public hazards in the world today, and in time clearing up and dispose rubbish is to build graceful, clean and tidy, civilized modern city conditio sune qua non.The valid approach that solves garbage problem is with waste reductionization, resource utilization, innoxious.Many organic compositions are arranged in the rubbish, and that uses manufactures fertilizer and can turn waste into wealth.But,, can cause problems such as unevenness of application, stench, even can cause environment to pollute once more if directly adopt methods such as landfill.
Summary of the invention
The purpose of this utility model is for a kind of rubbish hydrolysis device is provided.
For realizing the purpose of this utility model, this specification sheets provides a kind of hydrolytic decomposition pot, the cylindrical shell that comprises cylindricality, the cylindrical shell top connects elipse head, the elipse head center is provided with dog-house, also be provided with safety valve and vent valve on the elipse head, the cylindrical shell below connects taper and takes over, taper is taken over the center and is provided with discharge port, and discharge port is provided with the outlet pneumavalve, steam valve, water discharge valve, taper adapter and cylindrical shell junction are provided with the air intake valve, the air intake valve connects airduct, airduct coils in taper is taken over, and the cylindrical shell side is provided with porthole, porthole, vent valve, air intake valve place all is equipped with tensimeter and thermometer.
Use this hydrolytic decomposition pot to produce, first check valve, closed safe valve, vent valve, outlet pneumavalve and steam valve; Begin from the dog-house charging; When being fed to cylindrical shell volumetrical 20%, open steam valve, temperature is risen gradually,, discharge water of condensation, be not less than in 50 environment of spending in temperature and continue charging above opening water discharge valve behind 50 degree; After being fed to cylindrical shell and being full of, the residual foreign material of cleaning opening for feed, close the opening for feed valve, the turn-off time was controlled at 10 ± 2 minutes, closed water shoot; The steam off valve is opened vent valve and is carried out emptying, and emptying time is 15 minutes, simultaneously hydrolytic decomposition pot is imported and exported check; Close vent valve after emptying is finished and open steam valve and boost, the air valve that begins to rehearse heats up, through boost for four times, after the exhaust, temperature-rise period, pressure reaches 1.1MPa, when temperature reached 185 ℃, heat-insulation pressure keeping was opened water discharge valve simultaneously and is accelerated draining; Draining to water displacement obviously reduces, and closes water discharge valve when being the slightly thick shape of amaranth and finishes draining; The air valve that begins to rehearse has been arranged pressure in the jar; When pressure near 0 the time, close vent valve, open the discharge port operated pneumatic valve, spray quick-fried; After spraying quick-fried end, open vent valve 1, to pressure be 0, carry out twice repeatedly.
Boost, the pressure and temperature of the four-stage in the exhaust, temperature-rise period is,
Fs: boost after the emptying, to 0.3-0.35MPa, the time is 15 ± 2 minutes, and temperature is 140-145 ℃;
Subordinate phase: boost to 0.6-0.65MPa, the time is 8 ± 2 minutes, and temperature is 160-165 ℃;
Phase III: boost to 0.8-0.85MPa, the time is that 5 ± 1 minutes temperature are 170-175 ℃;
The quadravalence section: boost to 1.0-1.1MPa, the time is 5 ± 1 minutes, and temperature is 180-185 ℃.
This hydrolytic decomposition pot and technology thereof successfully are transplanted to the fermentative production technology in the modern biological-pharmacy in the production of organic fertilizer fermentation reactor system, not only greatly shorten the production cycle, and had fermentation complete decomposition, safety, health, reliable, advantage such as dehydrating effect is good.
This technology is with sieving garbage, and the organic waste that sub-elects enters the hydrolytic decomposition pot hydrolysis.Under water vapor and High Temperature High Pressure; hemicellulose deacetylation in the rubbish organic matter produces acetic acid and plays catalyst action; wherein starch dextrinize and oligose; cellulose conversion becomes short chain Mierocrystalline cellulose and oligose; protein transduction changes into peptide class and amino acid; hydrolysate sieves through spraying quick-fried after drying then; screen underflow accounts for 50% greatly; for brown powder shape darkly is the fertilizer of generation; add inorganic fertilizer such as urea etc. through batching; promptly formed compoiste fertilizer through granulation again, the generation that is destitute of smell of entire treatment process has reached the effect of municipal wastes utilization of waste as resource.
The purpose of this utility model, feature and advantage will be in conjunction with the embodiments, are further described with reference to accompanying drawing.
Description of drawings
Fig. 1 is a structural representation of the present utility model;
Wherein: 1 is cylindrical shell, and 2 is elipse head, and 3 is dog-house, and 4 is safety valve, and 5 is vent valve, and 6 are the taper adapter, and 7 is the air intake valve, and 8 is airduct, and 9 is porthole, and 10 is discharge port.
Embodiment
With reference to last figure, provide following embodiment.To help to understand the utility model by embodiment, but not limit content of the present utility model.All distortion that those of ordinary skill in the art can directly derive or associate from the disclosed content of the utility model all should be thought protection domain of the present utility model.
Embodiment: this hydrolytic decomposition pot, the cylindrical shell 1 that comprises cylindricality, cylindrical shell 1 top connects elipse head 2, elipse head 2 centers are provided with dog-house 3, also be provided with safety valve 4 and vent valve 5 on the elipse head 2, cylindrical shell 1 below connects taper and takes over 6, taper is taken over 6 centers and is provided with discharge port 10, discharge port 10 is provided with the outlet pneumavalve, steam valve, water discharge valve, taper adapter 6 and cylindrical shell 1 junction are provided with air intake valve 7, and air intake valve 7 connects airducts 8, and airduct 8 coils in taper to be taken in 6, cylindrical shell 1 side is provided with porthole 9, porthole 9, vent valve 5, air intake valve 7 places all are equipped with tensimeter and thermometer.
Claims (1)
1. hydrolytic decomposition pot, it is characterized in that: the cylindrical shell (1) that comprises cylindricality, cylindrical shell (1) top connects elipse head (2), elipse head (2) center is provided with dog-house (3), also be provided with safety valve (4) and vent valve (5) on the elipse head (2), cylindrical shell (1) below connects taper and takes over (6), taper is taken over (6) center and is provided with discharge port (10), discharge port (10) is provided with the outlet pneumavalve, steam valve, water discharge valve, (6) are taken in taper and cylindrical shell (1) junction is provided with air intake valve (7), air intake valve (7) connects airduct (8), airduct (8) coils in (6) are taken in taper, cylindrical shell (1) side is provided with porthole (9), porthole (9), vent valve (5), air intake valve (7) locates all to be equipped with tensimeter and thermometer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201067998U CN201065384Y (en) | 2007-03-01 | 2007-03-01 | Hydrolysis pot |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201067998U CN201065384Y (en) | 2007-03-01 | 2007-03-01 | Hydrolysis pot |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201065384Y true CN201065384Y (en) | 2008-05-28 |
Family
ID=39482555
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007201067998U Expired - Fee Related CN201065384Y (en) | 2007-03-01 | 2007-03-01 | Hydrolysis pot |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201065384Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102560554A (en) * | 2010-12-13 | 2012-07-11 | 贵阳铝镁设计研究院有限公司 | Distribution device for high pressure medium |
-
2007
- 2007-03-01 CN CNU2007201067998U patent/CN201065384Y/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102560554A (en) * | 2010-12-13 | 2012-07-11 | 贵阳铝镁设计研究院有限公司 | Distribution device for high pressure medium |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| DK177818B1 (en) | Process for treating a biomass with a lignocellulose content | |
| CN107513540A (en) | A kind of integrated form anaerobic ferment process and system | |
| CN104261907B (en) | The dry type anaerobic treatment method of rubbish from cooking | |
| CN101381674A (en) | Vertical non-stirred organic waste dry-type anaerobic digestion processing equipment and method | |
| GB2528611A (en) | Apparatus and process for treating waste | |
| CN102603144B (en) | Subcritical hydrothermal equipment for sludge treatment | |
| CN104588401A (en) | Forestry and agricultural residue skid-mounted module type component decomposition and separation equipment and method | |
| CN1583299A (en) | Life refuse treating process | |
| CN106906126A (en) | A kind of discarded fruits and vegetables anaerobic digestion and the system and method for marsh gas purifying purification | |
| CN201065384Y (en) | Hydrolysis pot | |
| CN101041596A (en) | Hydrolytic decomposition pot and technology thereof | |
| CN208679389U (en) | A kind of food waste treatment equipment convenient for cleaning | |
| CN202087572U (en) | Complete equipment used for resource recovery of kitchen garbage | |
| CN206858568U (en) | A kind of biogas natural pond fertilizer coproduction installation for fermenting | |
| CN109504724A (en) | Stalk cleans co-production technology | |
| CN202595133U (en) | Device for producing methane by utilizing Chinese medicament dregs | |
| CN202808632U (en) | Organic raw material preparation system of refuse fertilizer | |
| CN201644487U (en) | High-solid two-phase three-section biogas anaerobic digestion production device via perishable organic garbage | |
| CN208279524U (en) | A kind of environment-friendly deodorant refuse disposal installation | |
| CN202460584U (en) | High-temperature high-pressure sterilizing, hydrolyzing and curing reaction pot | |
| CN201404850Y (en) | Domestic garbage wet degradation reactor | |
| CN204564733U (en) | Agriculture and forestry organic waste material skid modular composition decomposition and separation equipment | |
| CN207685272U (en) | A kind of device for manufacturing generative fuel | |
| CN208250186U (en) | Hydrolysis hydrothermal oxidization kettle for garbage disposal | |
| CN206273814U (en) | A kind of organic solid waste processing 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: 20080528 Termination date: 20120301 |