CN204938217U - Material double automatic distributing and system of automatically fissioning - Google Patents
Material double automatic distributing and system of automatically fissioning Download PDFInfo
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- CN204938217U CN204938217U CN201520728698.9U CN201520728698U CN204938217U CN 204938217 U CN204938217 U CN 204938217U CN 201520728698 U CN201520728698 U CN 201520728698U CN 204938217 U CN204938217 U CN 204938217U
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- fission
- still
- fissioning
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- dolly
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Abstract
The utility model provides a kind of material double automatic distributing and system of automatically fissioning, and comprise two groups of parallel tracks, track is divided into fissile region, cloth district and discharge zone; Often organize track and be provided with the material dolly that one group of two ends is connected with winch; Cloth district is provided with double cloth system, flows to material dolly again after receiving material; Fissile region is provided with fission still, for the material entered in the material dolly of fission still being carried out High Temperature High Pressure fission process; Discharge zone is provided with discharging winch and material receiving conveyor, the compartment of discharging winch turnover trolley from the side, pours the material through fission process into material receiving conveyor, and downstream transport.The utility model adopts a series of automation equipment to combine, and degree of automation is high; And fission still adopts horizontal type structure, the mechanism such as compression indicator, safety valve and whole safe operation mechanism interlock, and improve the safety of system; Improve the transport process speed of organic waste.
Description
Technical field
The utility model relates to urban garbage treatment system, after rubbish material after metropolitan wastes sorting is carried out High Temperature High Pressure fission by it, carry out the automation equipment of harmless treatment, through the material of fission system process, by harmless, tasteless, for the making raw material of fertilizer and environment-friendly building materials, the utility model also relates to one can will select material high temperature high pressure process, thus reaches harmless, tasteless fission process.
Background technology
Along with the increase of urban population, municipal refuse output is increasing, also day by day serious to the harm of environment.With regard to China, the situation is tense for the problem of not only solid waste, and resource situation is also troubling, and per capita resources is lower than world standard, and degree of utilization is also very low.To the municipal refuse produced, best processing method is recover materials and the energy from rubbish, the i.e. resource of rubbish, thus realize rubbish subtract appearanceization, minimizing, innoxious and resource.
In municipal refuse, can pile rotten organic waste is one of main component in China's municipal refuse, comprises the foodstuff refuses such as leftovers leftovers, bone, dish green tops, pericarp.By the rotten organic matter of piling in rubbish, to carry out compost treatment be improve garbage regeneration to utilize the main path of level.By the compost treatment of rubbish, garbage as resource level can be significantly improved.
But the current organic waste composting technology of China mainly adopts mechanization compost and simple and easy During High-Temperature Composting technology, and facility is backwardness comparatively, long processing period, and industrialization degree is low, cause rubbish to become the low conversion rate of resource, and easily cause secondary pollution.Mainly there are three shortcomings in current mechanization compost and simple and easy During High-Temperature Composting technology:
1) composting technology resource conversion rate is low, is formed and wastes in a large number, and easily cause secondary pollution;
2) composting production produced is of low quality, fertilizer efficiency is lower, makes composting production slack market, finally causes dung yard to stop production because of overstocking of composting production;
3) working environment is filthy, and personal hygiene's guarantee condition is very severe.
Therefore, for the drawback of prior art, the utility model people is through studying for a long period of time, a kind of High Temperature High Pressure fission system and process and equipment thereof of automation are designed and developed, solve organic waste resourcable transformation and garbage disposal industrialization operation problem, the disposal and recovery for municipal refuse utilize automation process provide more economical, reliable, equip efficiently.
Utility model content
The purpose of this utility model is to provide a kind of material double automatic distributing and system of automatically fissioning, its systematicness is strong, degree of automation is high, working stability is reliable, be suitable for fission, hydrolysis that material completes material at high temperature under high pressure fast, generate the easily processed Small molecular carbon nitrogen compound of stable state, become the base-material being convenient to process further.
For achieving the above object, the technical solution adopted in the utility model is:
A kind of material double automatic distributing and system of automatically fissioning, it is characterized in that, comprise the two groups of tracks be arranged in parallel, two groups are divided into fissile region, discharge zone and cloth district with length;
Often organize track and be provided with the one group of material dolly that can connect, one end of each group material dolly is connected with into still winch, and the other end is connected with out still winch, enables this group of material dolly switching position between fissile region, cloth district and discharge zone;
Corresponding to the position in this cloth district, be provided with double cloth system, this double cloth system connects with jigging conveyer, flows to material dolly again after receiving material;
Corresponding to the position of this fissile region, be provided with fission still, for the material entered in the material dolly of fission still being carried out High Temperature High Pressure fission process;
Corresponding to the position of this discharge zone, be provided with discharging winch and material receiving conveyor, this discharging winch is used for the compartment of turnover trolley from the side, this material receiving conveyor is located at track side, for receiving the material through fission process gone out from the overturning of material dolly, and by the material downstream transport through fission process.
Described material double automatic distributing and system of automatically fissioning, wherein, this material dolly comprises the chassis and compartment that are connected by revolute pair, is walked in orbit by roller in chassis, compartment is provided with left armrests and right armrest, is also provided with front side serial mechanism and rear side serial mechanism.
Described material double automatic distributing and system of automatically fissioning, wherein, this compartment square steel tube does skeleton, and inner side A3 steel plate bends and is welded.
Described material double automatic distributing and system of automatically fissioning, wherein, this double cloth system comprises:
Frame, fixes on the ground, across above two groups of tracks;
Two position transdusers, are fixed on frame side, for detecting the seated position of the material dolly below frame on each group track;
Whether two super sonics completely expect monitoring device, are fixed on frame side, completely expect for the material dolly detected below frame on each group track;
Rotating distribution conveyor, it to be fixed in frame and to connect with jigging conveyer, and be respectively provided with a feeder below the two ends of this rotating distribution conveyor, two feeders are respectively used to the material dolly feeding on one group of track.
Described material double automatic distributing and system of automatically fissioning, wherein, this double cloth system also comprises material frame baffle plate, and it is fixed on the both sides of rotating distribution conveyor.
Described material double automatic distributing and system of automatically fissioning, wherein, one end of two groups of tracks is this fissile region, and the other end is this discharge zone, is this cloth district between two ends.
Described material double automatic distributing and system of automatically fissioning, wherein, this fission still has horizontal tank body, the two ends of tank body are equipped with compression indicator, forcing pipe and enter/drain pipe, this compression indicator is for measuring the force value in fission still, this forcing pipe is communicated with high temperature and high pressure steam, two this enter/drain pipe for fission still in inject/discharge cooling water expansion tank.
Described material double automatic distributing and system of automatically fissioning, wherein, tank body two ends left cover and right cover seal, and this tank body is connected sealing station with left cover and right cover and is provided with point of connection compression indicator, and this point of connection compression indicator is for measuring the force value of this connection sealing station.
Described material double automatic distributing and system of automatically fissioning, wherein, the two ends of tank body are equipped with safety valve, and this safety valve is for limiting the top pressure of this fission still.
Described material double automatic distributing and system of automatically fissioning, wherein, the two ends of tank body are equipped with glass tube level gauge, and this glass tube level gauge is used for condensed water in Real-Time Monitoring fission still and total electrolyte level of cooling water expansion tank.
Compared with prior art, the beneficial effect that the utility model has is:
1, the utility model adopts a series of automation equipment to combine, and degree of automation is high;
2, still of fissioning adopts horizontal type structure, and the mechanism such as compression indicator, safety valve and whole safe operation mechanism interlock, and improve the safety of system; Improve the transport process speed of organic waste;
3, the fission system adopted changes the technique of compost in the past, substantially increase and transform the production efficiency of producing fertilizer and the conformability that improve organic fertilizer quality, the research of the utility model product, effectively can promote the industrialization operation of garbage as resource recycle.
Accompanying drawing explanation
Fig. 1 is fission system process figure;
Fig. 2 is fission system process equipment planar view;
Fig. 3-1 is fission still structural representation;
Fig. 3-2 is fission still lateral plan;
Fig. 3-3 is fission still covering auto lock schematic diagram;
Fig. 3-4 is fission still gage glass schematic diagram;
Fig. 4-1 is material vehicle structure schematic diagram;
Fig. 4-2 is material dolly side schematic view;
Fig. 5-1 is double cloth system schematic diagram;
Fig. 5-2 is double cloth system birds-eye view.
Description of reference numerals: 1-enters still winch; 2-fissions still; 3-material dolly; 4-jigging conveyer; 5-double cloth system; 6-material receiving conveyor; 7-discharging winch; The total conveyer of 8-; 9-goes out still elevator conveyer; 201-point of connection compression indicator; 202-safety valve; 203-compression indicator; 204-forcing pipe; 205-fission still tank body; 206-fission still right cover; 207-enters/drain pipe; 208-fission still base; 209-fission still left cover; 210-safety and interlock device; 211-automatic locking mechanism; 212-worm and gear catch gear; 213-glass tube level gauge; 214-track; 301-compartment; 302-left armrests; 303-revolute pair; 304-cast iron roller; 305-chassis; 306-track; Serial mechanism on rear side of 308-; Serial mechanism on front side of 309-; 501-position transduser; 502-super sonic completely expects monitoring device; 503-feeder; 504-material frame baffle plate; 505-frame; 506-rotating distribution conveyor.
Detailed description of the invention
Fig. 1 describes the fission system process involved by the utility model, Fig. 2 is process equipment planar view of the present utility model, shown in composition graphs 1, Fig. 2, the material double automatic distributing that the utility model provides and system of automatically fissioning, comprise the two groups of tracks be arranged in parallel, one end of two groups of tracks is fissile region, and the other end is discharge zone, is cloth district between two ends;
Often organize track and be provided with one group of (the present embodiment is nine one group) the material dolly 3 that can connect, one end of each group material dolly 3 is connected with into still winch 1, the other end is connected with out still winch 9, make this group of material dolly 3 can between fissile region, cloth district and discharge zone switching position;
Corresponding to the position in this cloth district, be provided with double cloth system 5, this double cloth system 5 connects with jigging conveyer 4, flows to material dolly 3 again after receiving material;
Corresponding to the position of this fissile region, be provided with fission still 2, for the material entered in the material dolly 3 of fission still 2 being carried out High Temperature High Pressure fission process;
Corresponding to the position of this discharge zone, be provided with discharging winch 7, material receiving conveyor 6 and total conveyer 8, this discharging winch 7 is for the compartment of turnover trolley 3 from the side, this material receiving conveyor 6 is located at track side, for receiving the material through fission process gone out from material dolly 3 overturning, and give this total conveyer 8 by the mass transport through fission process.
When work, as shown in Figure 1, by jigging conveyer 4, material is inputted in double cloth system 5, position transduser detects that material dolly 3 has been located in cloth district, double cloth system 5 is feeded to material dolly 3 in place, after a material dolly 3 is filled, is just moved a certain distance by the material dolly 3 of connecting, another material dolly 3 is feeded, until this group material dolly 3 is all filled, the kettle cover of fission still 2 is opened, enter still winch 1 to start working, dragging this group material dolly 3 enters in fission still 2, enter still winch 1 to withdraw from, fission still 2 kettle cover is closed automatically, until connecting sensor monitors airtight, pipeline valve starts automatically, temperature-pressure in fission still 2, until reach design temperature and setting barometric pressure in fission still 2, fission systemic effect setting-up time (generally enters still 30 minutes, go out still 30 minutes, fission systemic effect 1 hour), after the fission systemic effect time arrives, blowdown valve effect, the pressure release of fission still 2, then connecting sensor effect, fission still 2 kettle cover is opened, go out still winch 9 to act on, this group material dolly 3 is hauled out, be dragged to discharge zone, series connection removed by this group material dolly 3, manually hang up discharging winch 7, make side, the compartment overturning of material dolly 3, thus the material after fission is poured on material receiving conveyor 6, again by total conveyer 8 by fission after mass transport to treatment process below, after material unsnatched by a material dolly 3, discharging winch 7 moves forward a position, make next material dolly 3 in place, circulation like this, until this group material dolly 3 is all unsnatched, then this group material dolly 3 is connected, enter still winch 1 and act on, again this group material dolly 3 is drawn to cloth district, so move in circles work,
As shown in Figure 2, when the material dolly 3 on a wherein track fission to enter fission process in still 2 time, the material dolly 3 on another track carries out discharging work and cloth work, and alternation like this, enhances productivity.
Referring again to Fig. 3-1, Fig. 3-2, Fig. 3-3 and Fig. 3-4, the structural representation of the fission still 2 that the utility model provides, it has horizontal tank body 205, tank body 205 two ends left cover 209 and right cover 206 seal, a left side is provided with bottom tank body 205, in, right three groups of bases 208 are (left, right base 208 is firm banking 208, central seat 208 is mobile base 208), the two ends of tank body 205 are equipped with point of connection compression indicator 201, safety valve 202, compression indicator 203, forcing pipe 204, enter/drain pipe 207, safety and interlock device 210, automatic locking mechanism 211, worm and gear catch gear 212 and glass tube level gauge 213, wherein:
This point of connection compression indicator 201 to be connected the force value of sealing station with left cover 209 and right cover 206 for measuring fission still 2 inherent tank body 205;
This safety valve 202 is for limiting the top pressure of this fission still 2, if exceed this top pressure, then safety valve 202 is opened, and reduces the pressure in fission still 2;
This compression indicator 203 is for measuring the force value in fission still 2;
This forcing pipe 204 is communicated with high temperature and high pressure steam (as boiler), inputs high temperature and high pressure steam, provide the environment of the fission needed for material by this forcing pipe 204 to fission still 2;
Two this enter/drain pipe 207 for injecting/discharging a certain amount of cooling water expansion tank in fission still 2, after still 2 completes predetermined fission process operation when fission, realize the quick cooling of fission system, step-down;
This safety and interlock device 210, this automatic locking mechanism 211 are necessary safety devices;
This glass tube level gauge 213 is for the condensed water in Real-Time Monitoring fission still 2 and total electrolyte level of cooling water expansion tank.
This fission still 2 working process is as follows:
Before starting working, right cover 206, left cover 209 are opened, enter the steel wire penetrating tank body 205 of still winch 1, tie up on material dolly 3, the material dolly 3 connected is moved in fission still 2 along track 214,306, the steel rope entering still winch 1 draws off fission still 2, right cover 206, left cover 209 are closed, safety and interlock device 210, automatic locking mechanism 211, worm and gear catch gear 212 act on, by airtight for whole fission still 2, add steam by forcing pipe 204, progressively reach the fission environment of required material High Temperature High Pressure.
In the fission process of whole material, monitor and forecast is carried out by point of connection compression indicator 201, safety valve 202, compression indicator 203, glass tube level gauge 213, the track 214 of material dolly 3 in fission still 2 and the track 306 in cloth district connect and leave gap (this gap as the activity space of left cover 206, right cover 209, but the enough little roller 304 of material dolly 3 that makes in this gap can not therefrom drop).
Go out still flow process: when after the process time that material reaches fission inside fission still 2, by entering/drain pipe 207 injects cooling water expansion tank, make fission still 2 pressure release, cooling, then, right cover 206, left cover 209 are opened, the material dolly 3 connected, on material dolly 3, is pulled out tank body 205 by the wire rope rope going out still winch 9.
Please continue to refer to Fig. 4-1 and Fig. 4-2, the structural representation of the material dolly 3 that the utility model provides, comprise the chassis 305 and compartment 301 that are connected by revolute pair, walked on track 306 by cast iron roller 304 in chassis 305, compartment 301 does skeleton with square steel tube, inner side A3 steel plate bends and is welded, and compartment 301 is provided with left armrests 302 and right armrest 307, is also provided with front side serial mechanism 309 and rear side serial mechanism 308.
After discharge zone moved to by material dolly 3, first the material dolly 33 of series connection is taken apart, again by the wire rope rope of discharging winch 7 in the right armrest 307 of logistics trolley, discharging winch 7 works, steel rope pulls the compartment 301 of material dolly 3 to rotate around revolute pair, material in material dolly 3 is poured on material receiving conveyor 6, then delivers to next treatment process through total conveyer 8.Unsnatch the material of a material dolly 3, then mobile discharge winch 7, unload next material dolly 3, after all unsnatching, then material dolly 3 is cascaded.
Please then consult Fig. 5-1, Fig. 5-2, be the structural representation of the double cloth system 5 that the utility model provides, comprise:
Frame 505, fixes on the ground with expansion bolt, across above two groups of tracks 501;
Two position transdusers 501, are fixed on frame 505 side, for detecting the seated position of the material dolly 3 below frame 505 on each group track 501;
Whether two super sonics completely expect monitoring device 502, are fixed on frame 505 side, completely expect for the material dolly 3 detected below frame 505 on each group track 501;
Rotating distribution conveyor 506, it to be fixed in frame 505 and to connect with jigging conveyer 4, is respectively provided with a feeder 503, two feeders 503 and is respectively used to material dolly 3 feeding on one group of track below the two ends of this rotating distribution conveyor 506;
Material frame baffle plate 504, is fixed on the both sides of rotating distribution conveyor 506, drops from the side of rotating distribution conveyor 506 for preventing material.
Time double cloth system 5 works, material is inputted by jigging conveyer 4, fall on rotating distribution conveyor 506, according to the signal prompt of position transduser 501, rotating distribution conveyor 506 is guided to run to correct direction, injecting material in the logistics trolley put in place, after super sonic completely expects that monitoring device 502 monitors full material, rotating distribution conveyor 506 operation suspension, if rotating distribution conveyor 506 receives the signal of another set of position transduser 501, then inverted running, to material dolly 3 injecting material on another group track.
Feature of the present utility model
1, the utility model adopts a series of automation equipment to combine, and degree of automation is high;
2, still of fissioning adopts horizontal type structure, and the mechanism such as compression indicator, safety valve and whole safe operation mechanism interlock, and improve the safety of system; Improve the transport process speed of organic waste;
3, the fission system adopted changes the technique of compost in the past, substantially increase and transform the production efficiency of producing fertilizer and the conformability that improve organic fertilizer quality, the research of the utility model product, effectively can promote the industrialization operation of garbage as resource recycle.
Claims (10)
1. material double automatic distributing and a system of automatically fissioning, is characterized in that, comprises the two groups of tracks be arranged in parallel, and two groups are divided into fissile region, discharge zone and cloth district with length;
Often organize track and be provided with the one group of material dolly that can connect, one end of each group material dolly is connected with into still winch, and the other end is connected with out still winch, enables this group of material dolly switching position between fissile region, cloth district and discharge zone;
Corresponding to the position in this cloth district, be provided with double cloth system, this double cloth system connects with jigging conveyer, flows to material dolly again after receiving material;
Corresponding to the position of this fissile region, be provided with fission still, for the material entered in the material dolly of fission still being carried out High Temperature High Pressure fission process;
Corresponding to the position of this discharge zone, be provided with discharging winch and material receiving conveyor, this discharging winch is used for the compartment of turnover trolley from the side, this material receiving conveyor is located at track side, for receiving the material through fission process gone out from the overturning of material dolly, and by the material downstream transport through fission process.
2. material double automatic distributing according to claim 1 and system of automatically fissioning, it is characterized in that, this material dolly comprises the chassis and compartment that are connected by revolute pair, walked in orbit by roller in chassis, compartment is provided with left armrests and right armrest, is also provided with front side serial mechanism and rear side serial mechanism.
3. material double automatic distributing according to claim 2 and system of automatically fissioning, is characterized in that, this compartment square steel tube does skeleton, and inner side A3 steel plate bends and is welded.
4. material double automatic distributing according to claim 1 and system of automatically fissioning, is characterized in that, this double cloth system comprises:
Frame, fixes on the ground, across above two groups of tracks;
Two position transdusers, are fixed on frame side, for detecting the seated position of the material dolly below frame on each group track;
Whether two super sonics completely expect monitoring device, are fixed on frame side, completely expect for the material dolly detected below frame on each group track;
Rotating distribution conveyor, it to be fixed in frame and to connect with jigging conveyer, and be respectively provided with a feeder below the two ends of this rotating distribution conveyor, two feeders are respectively used to the material dolly feeding on one group of track.
5. material double automatic distributing according to claim 4 and system of automatically fissioning, is characterized in that, this double cloth system also comprises material frame baffle plate, and it is fixed on the both sides of rotating distribution conveyor.
6. material double automatic distributing according to claim 1 and system of automatically fissioning, is characterized in that, one end of two groups of tracks is this fissile region, and the other end is this discharge zone, is this cloth district between two ends.
7. material double automatic distributing according to claim 1 and system of automatically fissioning, it is characterized in that, this fission still has horizontal tank body, the two ends of tank body are equipped with compression indicator, forcing pipe and enter/drain pipe, this compression indicator is for measuring the force value in fission still, this forcing pipe is communicated with high temperature and high pressure steam, two this enter/drain pipe for fission still in inject/discharge cooling water expansion tank.
8. material double automatic distributing according to claim 7 and system of automatically fissioning, it is characterized in that, tank body two ends left cover and right cover seal, this tank body is connected sealing station with left cover and right cover and is provided with point of connection compression indicator, and this point of connection compression indicator is for measuring the force value of this connection sealing station.
9. material double automatic distributing according to claim 7 and system of automatically fissioning, it is characterized in that, the two ends of tank body are equipped with safety valve, and this safety valve is for limiting the top pressure of this fission still.
10. material double automatic distributing according to claim 7 and system of automatically fissioning, it is characterized in that, the two ends of tank body are equipped with glass tube level gauge, and this glass tube level gauge is used for condensed water in Real-Time Monitoring fission still and total electrolyte level of cooling water expansion tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520728698.9U CN204938217U (en) | 2015-09-21 | 2015-09-21 | Material double automatic distributing and system of automatically fissioning |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520728698.9U CN204938217U (en) | 2015-09-21 | 2015-09-21 | Material double automatic distributing and system of automatically fissioning |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204938217U true CN204938217U (en) | 2016-01-06 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520728698.9U Expired - Fee Related CN204938217U (en) | 2015-09-21 | 2015-09-21 | Material double automatic distributing and system of automatically fissioning |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204938217U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106542279A (en) * | 2015-09-21 | 2017-03-29 | 冉文学 | Material double automatic distributing and system of fissioning automatically |
-
2015
- 2015-09-21 CN CN201520728698.9U patent/CN204938217U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106542279A (en) * | 2015-09-21 | 2017-03-29 | 冉文学 | Material double automatic distributing and system of fissioning automatically |
| CN106542279B (en) * | 2015-09-21 | 2018-11-09 | 云南财经大学 | Material double-station automatic distributing and system of fissioning automatically |
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| Date | Code | Title | Description |
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| 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: 20160106 Termination date: 20190921 |
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| CF01 | Termination of patent right due to non-payment of annual fee |