CN205115313U - Quick curing treatment facility of anaerobism natural pond sediment - Google Patents
Quick curing treatment facility of anaerobism natural pond sediment Download PDFInfo
- Publication number
- CN205115313U CN205115313U CN201520831879.4U CN201520831879U CN205115313U CN 205115313 U CN205115313 U CN 205115313U CN 201520831879 U CN201520831879 U CN 201520831879U CN 205115313 U CN205115313 U CN 205115313U
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- air
- natural pond
- waste gas
- blast
- air inlet
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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
- 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
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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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
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- Processing Of Solid Wastes (AREA)
Abstract
The utility model discloses a quick curing treatment facility of anaerobism natural pond sediment, the output of air inlet valve and the output of waste gas air inlet valve are connected respectively to the input of air -blast device, and the input of waste gas air inlet valve passes through the trunk line and connects air chamber one side, and heat transfer device's the input and the input of waste gas play blast gate are connected respectively to the output of air -blast device, heat transfer device's input is still connected hot water and is supplied water, and hot -blast blast gate input is connected all the way to heat transfer device's output, and hot -blast blast gate output passes through the trunk line and connect air chamber one side, and the temperature control valve input is connected on another way of heat transfer device's output, and the trunk line is connected to the temperature control valve output, the air chamber opposite side passes through tuber pipe and anaerobism natural pond slag muck storehouse intercommunication, this air inlet valve, hot -blast blast gate, waste gas air inlet valve, waste gas play blast gate, air -blast device, heat transfer device and temperature control valve are controlled by PLC. The utility model discloses can fast curing anaerobism natural pond sediment, shorten the curing time, reduce the curing energy consumption.
Description
Technical field
The utility model relates to anaerobism natural pond Slag treatment technical field, refers in particular to a kind of anaerobism natural pond slag rapid aging treatment facility.
Background technology
The anaerobic ferment process being raw material along with domestic organic garbage, changing food waste, feces of livestock and poultry, agricultural wastes, garden garbage etc. reaches its maturity.This organic substance had not only realized harmless treatment at anaerobic fermentation process, also obtained clean energy biogas simultaneously, but also to have improved the ecological environment and natural pond slag that anaerobically fermenting produces can develop the organic fertilizer of high-quality, be applied to farmland, improvement soil, increase soil fertility.
Anaerobic ferment process is varied, is divided into wet method anaerobically fermenting and dry-type anaerobic fermentation by its solids content; Be divided into by the type of device or technique: vertical type fermentation, horizontal fermentation etc.But which kind of anaerobically fermenting mode, finally all can produce natural pond slag and natural pond liquid, slag appropriate disposal and utilization in natural pond realizes last ring that anaerobically fermenting integrated artistic runs.
The effects such as anaerobic fermentation residue is rich in various plants nutrient, can fertilizing soil, improvement soil, have very high utility value.But in typical circumstances, because anaerobically fermenting secondary fermentation residue water ratio is higher, be unfavorable for directly using; In addition according to different fermentations technique, after anaerobically fermenting, undegradable organic content differs, especially wet-fermentation exist waterpower short circuit cause discharging exist be mixed into fresh non-fermentation materials, directly use will there will be burn seedling, contaminate environment risk.
Therefore need fresh natural pond slag is carried out to abundant slaking, improves its stability and the property used, by process, the production of anaerobic fermentation residue fast Development is become stable, efficient, safe and wieldy organic fertilizer, this case produces thus.
Utility model content
The purpose of this utility model is to provide a kind of anaerobism natural pond slag rapid aging treatment facility, with rapid aging anaerobism natural pond slag, shortens the curing time, reduces slaking energy consumption.
For reaching above-mentioned purpose, solution of the present utility model is:
A kind of anaerobism natural pond slag rapid aging treatment facility, comprises air inlet valve, hot blast outlet valve, waste gas air inlet valve, waste gas outlet valve, air-blast device, heat-exchanger rig, temperature control valve and air chamber; The input terminus of air-blast device connects the output terminal of air inlet valve and the output terminal of waste gas air inlet valve respectively, the input terminus of waste gas air inlet valve connects air chamber side by main pipeline, and the output terminal of air-blast device connects the input terminus of heat-exchanger rig and the input terminus of waste gas outlet valve respectively; The input terminus of heat-exchanger rig also connects hot water and supplies water, output terminal one tunnel of heat-exchanger rig connects hot blast outlet valve input terminus, hot blast outlet valve output terminal connects air chamber side by main pipeline, another road of the output terminal of heat-exchanger rig connects temperature control valve input terminus, and temperature control valve output terminal connects main pipeline; Air chamber opposite side is communicated with slag muck storehouse, anaerobism natural pond by airduct; This air inlet valve, hot blast outlet valve, waste gas air inlet valve, waste gas outlet valve, air-blast device, heat-exchanger rig and temperature control valve are controlled by PLC.
Further, air-blast device connects frequency transformer, and frequency transformer connects PLC.
Further, heat exchange tapping valve is set at heat-exchanger rig output terminal.
Further, the connecting tube of temperature control valve output terminal and main pipeline installs thermometric instrument.
Further, setting pressure instrument on main pipeline.
Further, bottom air chamber, install draw-off pump, discharge opeing delivery side of pump is connected to air chamber outside.
Further, control valve installed by the airduct connecting air chamber and slag muck storehouse, anaerobism natural pond.
A kind of anaerobism natural pond slag rapid aging treatment process, comprises the following steps:
One, carry out interval type to slag muck storehouse, anaerobism natural pond and send hot blast, wind is delivered to heat-exchanger rig by air-blast device and carries out heat exchange generation by this hot blast, and air-blast device and heat-exchanger rig are controlled by PLC; Or carry out interval type to slag muck storehouse, anaerobism natural pond and send natural wind, this natural wind is delivered to slag muck storehouse, anaerobism natural pond by air-blast device, and air-blast device is controlled by PLC; Or first interval type is carried out to slag muck storehouse, anaerobism natural pond and send hot blast, wind is delivered to heat-exchanger rig by air-blast device and carries out heat exchange generation by this hot blast, air-blast device and heat-exchanger rig are controlled by PLC, again interval type is carried out to slag muck storehouse, anaerobism natural pond and send natural wind, this natural wind is delivered to slag muck storehouse, anaerobism natural pond by air-blast device, and air-blast device is controlled by PLC;
Two, detect the slag slaking of heap storage anaerobism natural pond and whether complete, then do not continue step one, after slaking completes, utilize air-blast device by the waste gas sucking-off in slag muck storehouse, anaerobism natural pond.
Further, the temperature of this hot blast is 55-75 DEG C.
Further, air-blast device air-supply is intermittent type: air-supply-suspend-air-supply-suspend.
After adopting such scheme, the utility model operationally, can selection mode A rapid aging pattern: open air inlet valve, close waste gas outlet valve, open hot blast outlet valve, close waste gas air inlet valve, run air-blast device, start heat-exchanger rig heat exchange, open temp control valve and regulate aperture, heat-exchanger rig passes into hot water; Wind enters heat-exchanger rig heat exchange through air-blast device, and hot blast regulates the laggard air inlet chamber of temperature through hot water, and liquid storage is in air chamber, and hot blast sends into slag muck storehouse, anaerobism natural pond through airduct.
In this pattern anaerobism natural pond slag, organic matter almost decomposes entirely, by gas blower, drop into fresh wind to heap storage, after heat exchange for hot run test, under the effect of hot run test, make natural pond slag rapid aging, decomposition, reach slaking.Slaking be operating as intermittent type: air-supply-suspend-air-supply-suspend.
Can selection mode B: open air inlet valve, close waste gas outlet valve, open hot blast outlet valve, close waste gas air inlet valve, air-blast device runs, close heat-exchanger rig heat exchange, closing temperature control valve, heat-exchanger rig do not pass into hot water; Natural wind enters in air chamber through air-blast device, and after through airduct send into slag muck storehouse, anaerobism natural pond.
Containing more undecomposed organic matter in this pattern natural pond slag, by gas blower, drop into fresh wind to heap storage, make natural pond slag be converted into aerobic mode by anaerobism mode, be decomposed organic matter further.Slaking be operating as intermittent type: air-supply-suspend-air-supply-suspend.
Also can selection mode A and Mode B successively.
Selection mode C after the slag slaking of anaerobism natural pond completes: close new air inlet valve, open waste gas outlet valve, close hot blast outlet valve, open waste gas air inlet valve, air-blast device runs, heat-exchanger rig cuts out, temperature control valve cuts out; Waste gas in slag muck storehouse, anaerobism natural pond enters air chamber through airduct, by air chamber through waste gas air inlet valve, then runs through air-blast device, is discharged by waste gas outlet valve.Operating characteristics is intermittent type: selection setting-startup air draught-suspend-exit.
The utility model fundamentally solves the random problem of natural pond slag rapid aging and running cost is reduced, and has following useful effect:
One, controlled by different air supply patterns, make full use of material characteristic, make the slaking reaction time shorten of natural pond slag.
Two, compared with complete drying technology, organic matter is fully degraded, and heating energy consumption significantly reduces.
Three, by air blowing control, control to precisely by slaking, pressure, temperature, moisture etc. are all detected.
Four, be applicable to the maturation process of all kinds of organic materials anaerobism natural ponds slag.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Label declaration
Air inlet valve 11 hot blast outlet valve 12
Waste gas air inlet valve 13 waste gas outlet valve 14
Air-blast device 2 frequency transformer 21
Heat-exchanger rig 3 heat exchange tapping valve 31
Temperature control valve 4 air chamber 5
Draw-off pump 51 main pipeline 6
Manometer 61 thermometric instrument 7
Airduct 8 heap storage 9
Control valve 91.
Embodiment
Below in conjunction with drawings and the specific embodiments, the utility model is described in detail.
Consult shown in Fig. 1, a kind of anaerobism natural pond slag rapid aging treatment facility that the utility model discloses, comprise air inlet valve 11, hot blast outlet valve 12, waste gas air inlet valve 13, waste gas outlet valve 14, air-blast device 2, heat-exchanger rig 3, temperature control valve 4 and air chamber 5.
The input terminus of air-blast device 2 connects the output terminal of air inlet valve 11 and the output terminal of waste gas air inlet valve 13 respectively, the input terminus of waste gas air inlet valve 13 connects air chamber 5 side by main pipeline 6, the input terminus of air inlet valve 11 connects air, and the output terminal of this waste gas air inlet valve 13 is connected on the pipeline between the output terminal of air inlet valve 11 and air chamber 5 input terminus.
The output terminal of air-blast device 2 connects the input terminus of heat-exchanger rig 3 and the input terminus of waste gas outlet valve 14 respectively, and the output terminal of waste gas outlet valve 14 connects exhaust pipeline.
The input terminus of heat-exchanger rig 3 also connects hot water and supplies water, output terminal one tunnel of heat-exchanger rig 3 connects hot blast outlet valve 12 input terminus, hot blast outlet valve 12 output terminal connects air chamber 5 side by main pipeline 6, another road of the output terminal of heat-exchanger rig 3 connects temperature control valve 4 input terminus, and temperature control valve 4 output terminal connects main pipeline 6.The connecting tube of temperature control valve 4 output terminal and main pipeline 6 installs thermometric instrument 7, regulates the aperture of temperature control valve 4 according to thermometric instrument 7 display data.Setting pressure instrument 61 on main pipeline 6 simultaneously.
Air chamber 5 opposite side is communicated with slag muck storehouse, anaerobism natural pond 9 by airduct 8.Control valve 91 installed by the airduct 8 connecting air chamber 5 and slag muck storehouse, anaerobism natural pond 9.This air inlet valve 11, hot blast outlet valve 12, waste gas air inlet valve 13, waste gas outlet valve 14, air-blast device 2, heat-exchanger rig 3 and temperature control valve 4 are not shown by PLC() control.
In the present embodiment, air-blast device 2 connects frequency transformer 21, and frequency transformer 21 connects PLC.The control and regulation of air quantity, blast when being realized commutation and the work of air-valve by the driving of PLC control system and frequency transformer 21.
Arrange heat exchange tapping valve 31 at heat-exchanger rig 3 output terminal, the liquid produced in heat-exchanger rig 3 is discharged by heat exchange tapping valve 31.Meanwhile, install draw-off pump 51 bottom air chamber 5, the output terminal of draw-off pump 51 is connected to air chamber 5 outside, is discharged by the hot water in air chamber 5.
The utility model also discloses a kind of anaerobism natural pond slag rapid aging treatment process, comprises the following steps:
One, carry out interval type to slag muck storehouse, anaerobism natural pond and send hot blast, wind is delivered to heat-exchanger rig by air-blast device and carries out heat exchange generation by this hot blast, and air-blast device and heat-exchanger rig are controlled by PLC; Or carry out interval type to slag muck storehouse, anaerobism natural pond and send natural wind, this natural wind is delivered to slag muck storehouse, anaerobism natural pond by air-blast device, and air-blast device is controlled by PLC; Or first interval type is carried out to slag muck storehouse, anaerobism natural pond and send hot blast, wind is delivered to heat-exchanger rig by air-blast device and carries out heat exchange generation by this hot blast, air-blast device and heat-exchanger rig are controlled by PLC, again interval type is carried out to slag muck storehouse, anaerobism natural pond and send natural wind, this natural wind is delivered to slag muck storehouse, anaerobism natural pond by air-blast device, and air-blast device is controlled by PLC; The temperature of this hot blast is 55-75 DEG C; Air-blast device air-supply is intermittent type: air-supply-suspend-air-supply-suspend.
Two, detect the slag slaking of heap storage anaerobism natural pond and whether complete, then do not continue step one, after slaking completes, utilize air-blast device by the waste gas sucking-off in slag muck storehouse, anaerobism natural pond.
The utility model operationally, can selection mode A rapid aging pattern: open air inlet valve 11, close waste gas outlet valve 14, open hot blast outlet valve 12, close waste gas air inlet valve 13, run air-blast device 2, start heat-exchanger rig 3 heat exchange, open temp control valve 4 and regulate aperture, heat-exchanger rig 3 passes into hot water; Wind enters heat-exchanger rig 3 heat exchange through air-blast device 2, and hot blast regulates the laggard air inlet chamber 5 of temperature through hot water, and liquid storage is in air chamber 5, and hot blast sends into slag muck storehouse, anaerobism natural pond 9 through airduct 8.In this pattern anaerobism natural pond slag, organic matter almost decomposes entirely, by gas blower, drop into fresh wind to heap storage, after heat exchange for hot run test, under the effect of hot run test, make natural pond slag rapid aging, decomposition, reach slaking.Slaking be operating as intermittent type: air-supply-suspend-air-supply-suspend.
Can selection mode B: open air inlet valve 11, close waste gas outlet valve 14, open hot blast outlet valve 12, close waste gas air inlet valve 13, air-blast device 2 runs, close heat-exchanger rig 3 heat exchange, closing temperature control valve 4, heat-exchanger rig 3 do not pass into hot water; Natural wind enters in air chamber 5 through air-blast device 2, and after send into slag muck storehouse, anaerobism natural pond 9 through airduct 8.Containing more undecomposed organic matter in this pattern natural pond slag, by gas blower, drop into fresh wind to heap storage, make natural pond slag be converted into aerobic mode by anaerobism mode, be decomposed organic matter further.Slaking be operating as intermittent type: air-supply-suspend-air-supply-suspend.
Also can selection mode A and Mode B successively.Selection mode C after the slag slaking of anaerobism natural pond completes: close new air inlet valve 11, open waste gas outlet valve 14, close hot blast outlet valve 12, open waste gas air inlet valve 13, air-blast device 2 runs, heat-exchanger rig 3 cuts out, temperature control valve 4 cuts out; Waste gas in slag muck storehouse, anaerobism natural pond 9 enters air chamber 5 through airduct 8, by air chamber 5 through waste gas air inlet valve 13, then runs through air-blast device 2, is discharged by waste gas outlet valve 14.Operating characteristics is intermittent type: selection setting-startup air draught-suspend-exit.
The foregoing is only preferred embodiment of the present utility model, not to the restriction of this case design, all equivalent variations done according to the design key of this case, all fall into the protection domain of this case.
Claims (7)
1. an anaerobism natural pond slag rapid aging treatment facility, is characterized in that: comprise air inlet valve, hot blast outlet valve, waste gas air inlet valve, waste gas outlet valve, air-blast device, heat-exchanger rig, temperature control valve and air chamber; The input terminus of air-blast device connects the output terminal of air inlet valve and the output terminal of waste gas air inlet valve respectively, the input terminus of waste gas air inlet valve connects air chamber side by main pipeline, and the output terminal of air-blast device connects the input terminus of heat-exchanger rig and the input terminus of waste gas outlet valve respectively; The input terminus of heat-exchanger rig also connects hot water and supplies water, output terminal one tunnel of heat-exchanger rig connects hot blast outlet valve input terminus, hot blast outlet valve output terminal connects air chamber side by main pipeline, another road of the output terminal of heat-exchanger rig connects temperature control valve input terminus, and temperature control valve output terminal connects main pipeline; Air chamber opposite side is communicated with slag muck storehouse, anaerobism natural pond by airduct; This air inlet valve, hot blast outlet valve, waste gas air inlet valve, waste gas outlet valve, air-blast device, heat-exchanger rig and temperature control valve are controlled by PLC.
2. a kind of anaerobism natural pond as claimed in claim 1 slag rapid aging treatment facility, is characterized in that: air-blast device connects frequency transformer, and frequency transformer connects PLC.
3. a kind of anaerobism natural pond as claimed in claim 1 slag rapid aging treatment facility, is characterized in that: arrange heat exchange tapping valve at heat-exchanger rig output terminal.
4. a kind of anaerobism natural pond as claimed in claim 1 slag rapid aging treatment facility, is characterized in that: on the connecting tube of temperature control valve output terminal and main pipeline, install thermometric instrument.
5. a kind of anaerobism natural pond as claimed in claim 1 slag rapid aging treatment facility, is characterized in that: setting pressure instrument on main pipeline.
6. a kind of anaerobism natural pond as claimed in claim 1 slag rapid aging treatment facility, it is characterized in that: bottom air chamber, install draw-off pump, discharge opeing delivery side of pump is connected to air chamber outside.
7. a kind of anaerobism natural pond as claimed in claim 1 slag rapid aging treatment facility, is characterized in that: on the airduct connecting air chamber and slag muck storehouse, anaerobism natural pond, install control valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520831879.4U CN205115313U (en) | 2015-10-26 | 2015-10-26 | Quick curing treatment facility of anaerobism natural pond sediment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520831879.4U CN205115313U (en) | 2015-10-26 | 2015-10-26 | Quick curing treatment facility of anaerobism natural pond sediment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205115313U true CN205115313U (en) | 2016-03-30 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520831879.4U Withdrawn - After Issue CN205115313U (en) | 2015-10-26 | 2015-10-26 | Quick curing treatment facility of anaerobism natural pond sediment |
Country Status (1)
| Country | Link |
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| CN (1) | CN205115313U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105272432A (en) * | 2015-10-26 | 2016-01-27 | 厦门市联谊吉源环保工程有限公司 | Quick curing treatment equipment and treatment method of anaerobic biogas residue |
| CN111848258A (en) * | 2020-07-31 | 2020-10-30 | 兰州理工大学 | Biomass-to-gas-liquid solid fertilizer rapid conversion system |
-
2015
- 2015-10-26 CN CN201520831879.4U patent/CN205115313U/en not_active Withdrawn - After Issue
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105272432A (en) * | 2015-10-26 | 2016-01-27 | 厦门市联谊吉源环保工程有限公司 | Quick curing treatment equipment and treatment method of anaerobic biogas residue |
| CN105272432B (en) * | 2015-10-26 | 2018-07-13 | 厦门市联谊吉源环保工程有限公司 | A kind of anaerobism biogas residue rapid aging processing equipment and processing method |
| CN111848258A (en) * | 2020-07-31 | 2020-10-30 | 兰州理工大学 | Biomass-to-gas-liquid solid fertilizer rapid conversion system |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20160330 Effective date of abandoning: 20180713 |
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| AV01 | Patent right actively abandoned |