CN205110337U - Surplus kitchen garbage in kitchen processing apparatus that hydrolysises - Google Patents
Surplus kitchen garbage in kitchen processing apparatus that hydrolysises Download PDFInfo
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- CN205110337U CN205110337U CN201520773304.1U CN201520773304U CN205110337U CN 205110337 U CN205110337 U CN 205110337U CN 201520773304 U CN201520773304 U CN 201520773304U CN 205110337 U CN205110337 U CN 205110337U
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Abstract
The utility model discloses a surplus kitchen garbage in kitchen processing apparatus that hydrolysises, through pneumatic blow -off valve and off -load spouting silo explosion turn -on connection including hydrolysis treatment tank and the discharge gate of treatment tank of hydrolysising more than one and two, still including the hot dry wind gas holder, the input of hot dry wind gas holder is connected through the air bleeding valve and the top gas vent of the treatment tank of hydrolysising, still including setting up at the material hoist of treatment tank one side that hydrolysises, when hydrolysising the treatment tank more than two, the chevron shape tripper is installed to material hoist's top discharge gate below, and the material loops through chevron shape tripper, pneumatic feed valve, gets into the top feed inlet of the treatment tank of hydrolysising, the utility model discloses can can carry out the thorough innocent treatment of virus killing sterilization rapidly to above -mentioned two kinds rubbish under high pressure, high -temperature steam effect, under the effect of high temperature high pressure steam, all insect pests, virus, germ have pass out of existence, and two kinds of rubbish is by innocent treatment thoroughly, thoroughly part the inorganic matter that mixes in the middle of two kinds of rubbish with the organic matter.
Description
Technical field
Changing food waste hydrolysis process device more than hydrolysis draining technology field, particularly a kind of kitchen that the utility model relates to food garbage.
Background technology
Each district of China, cities and towns output every day ton up to a hundred and even thousands of tons of comprise the various organic wastes of the organic wastes such as changing food waste, rubbish from cooking, agricultural waste, aquaculture rubbish, various discarded fermentates; These organic wastes have formed the primary pollution source of current China urban and rural environment, seriously threaten modern city and towns and rural ecological environment.
Along with the development of national economy and improving constantly of people's life, in these years catering trade achieves swift and violent development, and pollution and the process problem of thing followed changing food waste have just become one of one of environmental protection work large emphasis problem; Due to changing food waste there is complicated component, greasy dirt is many, moisture is large, salinity high, is a very complicated problem to its process problem; Again because the large distribution of rubbish from cooking quantity is wide, moisture high humility is large, composition and complexity thereof, it has become major pollutants in the rubbish of town and country and pollution sources, and the macronucleus having become the many comprehensive resource processing items comprising waste incineration project is become or be suspicious difficult problem.
As everyone knows, comprise changing food waste, rubbish from cooking all organic wastes putrid and deteriorated after, all can produce foul gas, grow mosquitos and flies, produce bacterial virus to environment, jeopardize human health; Being the extremely urgent task of top priority to the improvement of these organic wastes, has been one of cardinal task of paying close attention to most of country, governments at all levels and even the whole society! The domestic process to these organic wastes has at present germinated many processes, such as: composting process (containing aerobic fermentation and anaerobic fermentation at interior bioanalysis), biogas method, pyrolytic gasification method, burning method, landfill method ...).
(actual is the low pressure steam of pressure about 1Mpa, temperature 150-200 DEG C to utilize high-pressure and high-temperature steam, technique custom is commonly called as " HTHP ") in hydrolysis process tank, at catalyst and the auxiliary lower rapid of additive, quick composting degraded (2-3 hour), thorough disinfection sterilizing are implemented to rubbish from cooking changing food waste, and then make these organic wastes change into high-quality organic matter, and then a kind of industrialization treatment technology equipment of recycling.
Utility model content
Technical problem to be solved in the utility model is, overcomes the shortcoming of prior art, provides changing food waste hydrolysis process device more than a kind of kitchen.
In order to solve above technical problem, the utility model provides changing food waste hydrolysis process device more than a kind of kitchen, comprise one to more than two hydrolysis process tank and the discharging opening of hydrolysis process tank by pneumatic blow-off valve with spray quick-fried off-load storehouse conducting be connected, also comprise hot dry wind air accumulator, the input of hot dry wind air accumulator is connected with the top exhaust outlet of hydrolysis process tank by air bleeding valve; Also comprise the conveyer being arranged on hydrolysis process tank side, except not being provided with during a hydrolysis process tank except herringbone tripper, during multiple stage hydrolysis process tank, the top discharging opening of conveyer is connected with the top charging aperture of hydrolysis process tank by herringbone tripper, air-actuated feeding valve successively, wherein;
Hydrolysis process tank comprises tank body, upper cover, low head and air inlet pipe, the upper end of upper cover is provided with charging aperture, the lower end of low head is discharging opening, charging aperture place is provided with the output that air-actuated feeding valve connects herringbone tripper, discharge outlet connects pneumatic blow-off valve by drainage conduit, tank body lower end sidewall offers air inlet, air inlet pipe stretches into tank interior by air intake valve, air inlet pipe is communicated with at least one air inlet endless tube, air inlet endless tube is successively set on low head from top to bottom near discharge outlet, air inlet endless tube is descending setting from top to bottom, connected by communicating pipe between each air inlet endless tube, upper cover upper end also offers exhaust outlet, and exhaust ports is provided with air bleeding valve,
Off-load spray wharf explosion comprises warehouse, drainage conduit, horizontal striker plate, Long Liao mechanism, longitudinal conveyer, horizontal conveyer and elevator, drainage conduit runs through warehouse one side side wall lower ends and arranges, horizontal striker plate is arranged on warehouse away from the sidewall of drainage conduit one end, longitudinal conveyer is arranged on below horizontal striker plate, the feed direction of longitudinal conveyer points to drainage conduit direction, horizontal conveyer is mutually vertical with the feed direction of longitudinal conveyer, horizontal conveyer one end is arranged on below longitudinal conveyer front end, horizontal conveyer runs through warehouse sidewall away from the other end of longitudinal conveyer and is connected with elevator,
Long Liao mechanism comprises motor and flitch is held together in two pieces of vertical revolutions, revolution holds together flitch between horizontal striker plate and longitudinal conveyer, the axisymmetrical that flitch longitudinally conveyer is held together in two pieces of revolutions is arranged, it is hinged by hinge that flitch one end and warehouse are held together in revolution, and the output shaft of motor holds together flitch along hinge reciprocating rotation by Chain conveyer drive revolution.
Technique effect: spray quick-fried off-load storehouse in the utility model and lead system by armored concrete and form, needs volume by 500-2000m according to treating capacity
3not etc., and the surge of 0.4-0.5Mpa can be born; The function of spraying quick-fried off-load storehouse mainly contain following some:
1. accept, unload, the material handled well is produced in the spray of temporary reactor;
The steam pressure of 2. off-load hydrolysis process tank;
3. unload, accept, hold the steam of being discharged by hydrolysis process tank;
4. in storehouse stock guide (cement causes or steel plate seam manufacture forms) guide and Long Liao mechanism common under, warehouse rear portion can be focused on spraying by hydrolysis process tank the material produced, then carry out rear operation process by a conveyer outside the material output storehouse handled well;
Hot dry wind air accumulator is a kind of low pressure vessel (0.1-0.6Mpa), it is that (temperature is at 150-180 for the steam of discharging with hydrolysis process tank self
0c), realize heat exchange with the normal temperature air compressed by air compressor and produce xeothermic compressed-air actuated process equipment, and then generating temperature at 120-150
0the xeothermic compressed air of about C.
The technical scheme that the utility model limits further is:
Further, changing food waste hydrolysis process device more than aforesaid kitchen, tank body is tubular, and tank interior is provided with level detector near the place at top.
Changing food waste hydrolysis process device more than aforesaid kitchen, the sidewall of tank body offers blowdown oilhole near tank body middle and lower part, and blowdown oilhole is communicated with blowdown fuel tap; Upper cover is dome head, low head can be spherical and conical end socket; Upper cover upper end is also provided with Pressure gauge and thermometer; Low head offers limber hole near discharge outlet, and limber hole is communicated with blowdown water valve.
Changing food waste hydrolysis process device more than aforesaid kitchen, the bottom of warehouse near the side of hinge higher than the side near drainage conduit; The bottom of warehouse offers the sewage collecting ditch with horizontal conveyer axis being parallel near the side of drainage conduit; Offer T-shaped foundation ditch at the bottom of storehouse in warehouse below horizontal stock guide, T-shaped foundation ditch width is greater than the width of longitudinal conveyer and horizontal conveyer, and longitudinal conveyer and horizontal conveyer are arranged in T-shaped foundation ditch.
Changing food waste hydrolysis process device more than aforesaid kitchen, is provided with receiving hopper in the T-shaped foundation ditch below horizontal striker plate, and the discharging opening of receiving hopper lower end is positioned at above horizontal conveyer, and longitudinal conveyer extend into the top of receiving hopper near horizontal conveyer one end.
Changing food waste hydrolysis process device more than aforesaid kitchen, warehouse offers door near drainage conduit place.
Changing food waste hydrolysis process device more than aforesaid kitchen, faces upward and is 5-15 ° with horizontal plane angle in drainage conduit discharge direction.
Changing food waste hydrolysis process device more than aforesaid kitchen, spraying quick-fried off-load storehouse is lead system by armored concrete to form, volume position 500-2000m
3, can bear the surge of 0.4-0.5Mpa, the pressure of hot dry wind air accumulator bears as 0.1-0.6Mpa.
The utility model is compared with prior art:
The utility model can to become thoroughly decomposed rapidly degraded (2-3 hour) to rubbish from cooking and changing food waste; Under high pressure, high-temperature steam effect, the harmless treatment thoroughly of rapid exterminating bacterium can be carried out to above-mentioned two kinds of rubbish; Under the effect of high temperature and high pressure steam, all insect pests, virus, germ have not existed, and two kinds of rubbish are by harmless treatment up hill and dale;
The utility model thoroughly can separate the inorganic matter be mingled in the middle of two kinds of rubbish with organic matter, so this technology is in industry also referred to as " heat choosing "; Its principle is:
Under high-temperature high-pressure craft state, all organic wastes are all become thoroughly decomposed degraded, macromolecular chain is broken into Small molecular chain, in the process of discharge with pressure (spraying quick-fried), can be fractured into Powdered under these effects of being pressed in self by the organic matter become thoroughly decomposed, and the inorganic matter be mingled in wherein, owing to being not enough to make it change physicochemical property and geometry state under this process conditions, still former state is discharged, be beneficial to the sorting (as screening) of downstream process to organic-inorganic thing with regard to pole like this, organic and inorganic matter are thoroughly separated;
Owing to there being the process of exhaust with pressure and sewer in technical process, within the water content of organic materials can be made to be down to 25-30%, reach certain dried material object;
Under the effect of high temperature and high pressure steam, the moisture in material, sump oil and material can be made to separate more up hill and dale.Under the effect of high temperature and high pressure steam, greasy dirt in organic materials will be swum in the surface of hydrolyzate in tank by diluting, as long as in material containing sump oil quantitative determination accurate, then a blowdown oil pipe is opened in the appropriate location on tube wall, just by outside sump oil more up hill and dale drain tank, thoroughly can be separated with sewage with organic materials by drain cock valve; The sewer valve at the bottom of tank is opened again, emptying manufacturability sewage (also claiming hydrolyzate) after emptying sump oil.So this process successfully can process changing food waste;
The utility model passivation, containing, flocculation, stripping can be mingled in free state heavy metal in organic waste; With the addition of a kind of under high-temperature acidic medium in the processing procedure of hydrolysis process tank, can react with free state heavy metal, and then passivation, containing, flocculation, stripping heavy metal, make flocculence heavy metal can flow in the middle of hydrolyzate along with condensed water, in the process of discharge hydrolyzate, most free state heavy metal is discharged hydrolysis process tank, and follow-up in the treatment process of hydrolyzate, carry out physics and chemistry process thoroughly, peel off heavy metal up hill and dale;
Because treatment process process of the present utility model uses high steam, in the process that hydrolyzate is formed, the salinity more than kitchen in changing food waste can be made fully to dissolve and be dissolved in the middle of hydrolyzate, and then with outside hydrolyzate drain tank, this just greatly reduces the salt content in material;
The utility model with the addition of a kind of catalyst in the charging process of hydrolysis process tank, and its effect is: the degraded of becoming thoroughly decomposed 1. accelerating organic waste; 2. promote the conversion of humic acid, monose, polysaccharide, improve organic quality; This technology just because of reactor, there is the incomparable technical advantage of other technology above-mentioned, so can be widely applied in the middle of the processing item to innoxious, the resource of the organic wastes such as the eutrophication pollutant of house refuse, changing food waste, agricultural waste, rivers and lakes.
Accompanying drawing explanation
The top view of changing food waste hydrolysis process device more than the kitchen of Fig. 1 designed by the utility model;
Fig. 2 is the sectional view in the A-A face of Fig. 1;
The structural representation of the hydrolysis process tank of changing food waste hydrolysis process device more than the kitchen of Fig. 3 designed by the utility model;
Wherein: 1-hydrolysis process tank, 101-charging aperture, 102-upper cover, 103-level detector, 104-blowdown fuel tap, 105-air inlet endless tube, 106-communicating pipe, 107-air inlet, 108-air inlet pipe, 109-air bleeding valve, 110-blowdown water valve, 2-conveyer, 3-hot dry wind air accumulator, 4-drainage conduit, 5-sprays quick-fried off-load storehouse, 501-drainage conduit, 502-warehouse, 503-door, the horizontal conveyer of 504-, 505-elevator, 506-T type foundation ditch, 507-Long Liao mechanism, flitch is held together in 507a-revolution, 507b-motor, 507c-rotating shaft, 507d-hinge, the longitudinal conveyer of 508-, the horizontal striker plate of 509-, 510-receiving hopper, 511-sewage collecting ditch, the pneumatic blow-off valve of 6-, 7-air-actuated feeding valve, 8-herringbone tripper.
Detailed description of the invention
embodiment 1
Structure as shown in Figure 1, changing food waste hydrolysis process device more than a kind of kitchen that the present embodiment provides, comprise at least two hydrolysis process tanks 1 and the discharging opening of hydrolysis process tank 1 by pneumatic blow-off valve 6 with spray quick-fried off-load storehouse 5 conducting be connected, also comprise hot dry wind air accumulator 3, the input of hot dry wind air accumulator 3 is connected with the top exhaust outlet of hydrolysis process tank 1 by air bleeding valve 109; Also comprise the conveyer 2 be arranged on hydrolysis process tank 1 limit, the top discharging opening of conveyer 2 is connected with the top charging aperture 101 of hydrolysis process tank 1 by herringbone tripper 8 air-actuated feeding valve 7 successively;
Hydrolysis process tank 1 comprises tank body, upper cover 102, low head and air inlet pipe, the upper end of upper cover 102 is provided with charging aperture 101, the lower end of low head is discharging opening, charging aperture 101 place is provided with the output that air-actuated feeding valve 7 connects herringbone tripper 8, discharge outlet connects pneumatic blow-off valve 6 by drainage conduit 4, tank body lower end sidewall offers air inlet, air inlet pipe 108 stretches into tank interior by intake valve 107, air inlet pipe connects 108 and is connected with at least one air inlet endless tube 105, air inlet endless tube 105 is successively set on low head from top to bottom near discharge outlet, air inlet endless tube 105 is descending setting from top to bottom, connected by communicating pipe 106 between each air inlet endless tube 105, upper cover 102 upper end also offers exhaust outlet, and exhaust ports is provided with air bleeding valve 109,
Off-load spray wharf explosion 5 comprises warehouse 502, drainage conduit 501, horizontal striker plate 509, Long Liao mechanism 507, longitudinal conveyer 508, horizontal conveyer 504 and elevator 505, drainage conduit 501 runs through warehouse 502 one side side wall lower ends and arranges, horizontal striker plate 509 is arranged on warehouse 502 away from the sidewall of drainage conduit 501 one end, longitudinal conveyer and horizontal conveyer are arranged in the T-shaped base ditch below horizontal striker plate, the feed direction of longitudinal conveyer points to drainage conduit direction, horizontal conveyer 504 is mutually vertical with the feed direction of longitudinal conveyer 508, horizontal conveyer 504 one end is arranged on below longitudinal conveyer 508 front end, horizontal conveyer 504 runs through warehouse 502 sidewall away from the other end of longitudinal conveyer 508 and is connected with elevator 505,
Long Liao mechanism 507 comprises motor 507b and two piece of vertical revolution and holds together flitch 507a, revolution holds together flitch 507a between horizontal striker plate 509 and longitudinal conveyer 508, the axisymmetrical that flitch 507a longitudinally conveyer 508 is held together in two pieces of revolutions is arranged, it is hinged by hinge 507d that flitch 507a one end and warehouse 502 are held together in revolution, and the output shaft of motor passes through Chain conveyer (or wire rope gearing) and drives revolution to hold together flitch 507a along hinge 507d reciprocating rotation;
Tank body is tubular, and tank interior is provided with level detector 103 near the place at top; The sidewall of tank body offers blowdown oilhole near tank body middle and lower part, and blowdown oilhole is communicated with blowdown fuel tap 104; Upper cover is dome head, and low head can be spherical or conical; Upper cover upper end is also provided with Pressure gauge and thermometer; Low head offers limber hole near discharge outlet, and limber hole is communicated with blowdown water valve 110;
The bottom of warehouse 502 near the side of hinge 507d higher than the side near drainage conduit 501; The bottom of warehouse 502 offers the sewage collecting ditch 511 with horizontal conveyer 504 axis being parallel near the side of drainage conduit 501; The below of the horizontal striker plate of warehouse 502 offers T-shaped foundation ditch 506, and T-shaped foundation ditch 506 width is greater than the width of longitudinal conveyer 508 and horizontal conveyer 504, and longitudinal conveyer 508 and horizontal conveyer 504 to be arranged in T-shaped foundation ditch 506;
Be provided with receiving hopper 510 in T-shaped foundation ditch 506 below horizontal striker plate 509, the discharging opening of receiving hopper 510 lower end is positioned at above horizontal conveyer 504, and longitudinal conveyer 508 stretches into the top of receiving hopper 510 near horizontal conveyer 504 one end; Warehouse 502 offers door 503 near drainage conduit 501 place; Face upward and be 5-15 ° with horizontal plane angle in drainage conduit 501 discharge direction; Spraying quick-fried off-load storehouse is lead system by armored concrete to form, volume position 500-2000m
3, can bear the surge of 0.4-0.5Mpa, the pressure of hot dry wind air accumulator bears as 0.1-0.6Mpa.
The treatment process of the present embodiment comprises following concrete steps:
before start, the air-actuated feeding valve of hydrolysis process tank charging aperture is in beyond open mode, and all the other each valves are all in closed condition;
The herringbone tripper of conveyer exit position is in the position to first canned material of hydrolysis process;
start first hydrolysis process tank, subsequently:
A: start to feed in hydrolysis process tank, when material is filled to 1/10 position of tank volume, open air intake valve, utilize hot dry wind air accumulator slowly to blast xeothermic compressed air towards reactor;
B: when material is filled to the 85-90% position of hydrolysis process tank volume, the air-actuated feeding valve closing of First hydrolysis process tank, air intake valve keeps opening, but xeothermic compressed air stopping blasts, open steam valve utilizes steam boiler slowly to blast high steam to hydrolysis process tank, enter boosting heating process, be specially:
One section: normal pressure rises to about 0.5 or 0.6Mpa, and temperature rises to 120 by normal temperature
o during about c, air intake valve is closed, drain tap is opened;
Exhaust step-down: pressure is down to 0.2 or 0.3Mpa by 0.6Mpa, when temperature is about down to about 60-80 DEG C, drain tap is closed, air intake valve is opened;
Two sections: air inlet boosting heats up again: pressure rises to 0.6 or 0.8Mpa by 0.2 or 0.3Mpa, when temperature about rises to about 150 DEG C, air intake valve is closed, drain tap is opened;
Exhaust step-down: pressure is down to 0.5 or 0.6Mpa by 0.8Mpa, when temperature is about down to 100 or 110 DEG C by 150 DEG C, drain tap is closed, air intake valve is opened;
Three sections: continue air inlet boosting and heat up: pressure rises to 0.9 or 0.95Mpa by 0.6Mpa, when temperature about rises to 185 DEG C; Air intake valve is closed, and system enters the pressure-maintaining and heat-preservation stage;
C: carry out pressure-maintaining and heat-preservation, process is about 1-1.5 hour;
D: exhaust pressure reduction: after pressure-maintaining and heat-preservation process terminates, open drain tap and transfer exhaust pressure reduction to, when Pressure Drop is to below 0.4Mpa, open the blowdown water valve under hydrolysis process tank tank, in blowdown vessel, condensation hydrolyzate is to Sewage Disposal, until Pressure Drop, to normal pressure, till obvious outwards exhaust outlet, closes blowdown water valve in tank;
E: the dehydration of hydrolysis material: the operating pressure of hydrolysis process tank is down to close to after " normal pressure ", close sewer valve, open intake valve, start in tank, inject xeothermic compressed air, injection length about controls at 30-40 minute, makes humidity of materials reduce to below 25-30%;
F: discharging process with pressure: discharging process with pressure is exactly after dehydration work step completes, close air bleeding valve, after continuing to inject xeothermic compressed air to 0.3-0.4Mpa pressure, close all valves of hydrolysis process tank, open pneumatic blow-off valve, material is sprayed quick-fried in drain charge cabin with pressure, then by feeding device, material is discharged outside storehouse;
If step F discharge is unclean, then repeats 1-2 time;
During the canned 85-90% position to hydrolysis process tank volume of First hydrolysis process, the stock guide in the herringbone tripper of conveyer discharge outlet is turned to opposite side, starts to second canned material of hydrolysis process, by that analogy;
In charging process, along with the continuous increase air intake valve opening of bed depth also increases gradually, admission pressure is increased gradually.
Above embodiment is only and technological thought of the present utility model is described; protection domain of the present utility model can not be limited with this; every technological thought according to the utility model proposes, any change that technical scheme basis is done, all falls within the utility model protection domain.
Claims (8)
1. changing food waste hydrolysis process device more than a kitchen, it is characterized in that, comprise more than 1 to two hydrolysis process tank (1) and the discharging opening of described hydrolysis process tank (1) is connected with spray quick-fried off-load storehouse (5) conducting by pneumatic blow-off valve (6), also comprise hot dry wind air accumulator (3), the input of described hot dry wind air accumulator (3) is connected with the top exhaust outlet of hydrolysis process tank (1) by air bleeding valve (109); Also comprise the conveyer (2) being arranged on hydrolysis process tank (1) side, described more than two during hydrolysis process tank, the top discharging opening of conveyer (2) is connected with the top charging aperture (101) of hydrolysis process tank (1) by herringbone tripper (8), air-actuated feeding valve (7) successively; If during a hydrolysis process tank, then do not need herringbone tripper;
Described hydrolysis process tank (1) comprises tank body, upper cover (102), low head and air inlet pipe, the upper end of described upper cover (102) is provided with charging aperture (101), the lower end of described low head is discharging opening, described charging aperture (101) place is provided with the output that air-actuated feeding valve (7) connects herringbone tripper (8), described discharge outlet connects pneumatic blow-off valve (6) by drainage conduit (4), described tank body lower end sidewall offers air inlet, described air inlet pipe (108) stretches into tank interior by intake valve (107), described air inlet pipe connects (108) and is connected with at least one air inlet endless tube (105), described air inlet endless tube (105) is successively set on low head from top to bottom near discharge outlet, the descending setting from top to bottom of described air inlet endless tube (105), connected by communicating pipe (106) between described each air inlet endless tube (105), described upper cover (102) upper end also offers exhaust outlet, and described exhaust ports is provided with air bleeding valve (109),
Described off-load spray wharf explosion (5) comprises warehouse (502), drainage conduit (501), horizontal striker plate (509), Long Liao mechanism (507), longitudinal conveyer (508), horizontal conveyer (504) and elevator (505), described drainage conduit (501) runs through described warehouse (502) one side side wall lower ends and arranges, described horizontal striker plate (509) is arranged on warehouse (502) away from the sidewall of drainage conduit (501) one end, described longitudinal conveyer is arranged on below horizontal striker plate, the feed direction of described longitudinal conveyer points to described drainage conduit direction, described horizontal conveyer (504) is mutually vertical with the feed direction of described longitudinal conveyer (508), described horizontal conveyer (504) one end is arranged on below described longitudinal conveyer (508) front end, described horizontal conveyer (504) is run through described warehouse (502) sidewall away from the other end of described longitudinal conveyer (508) and is connected with described elevator (505),
Described Long Liao mechanism (507) comprises motor (507b) and flitch (507a) is held together in two pieces of vertical revolutions, described revolution is held together flitch (507a) and is positioned between described horizontal striker plate (509) and described longitudinal conveyer (508), described two pieces of revolutions are held together flitch (507a) and are arranged along the axisymmetrical of described longitudinal conveyer (508), flitch (507a) one end is held together in described revolution and described warehouse (502) is hinged by hinge (507d), the output shaft of described motor drives described revolution to hold together flitch (507a) along hinge (507d) reciprocating rotation by Chain conveyer (or wire rope gearing).
2. changing food waste hydrolysis process device more than kitchen according to claim 1, it is characterized in that: described tank body is tubular, described tank interior is provided with level detector (103) near the place at top.
3. changing food waste hydrolysis process device more than kitchen according to claim 2, it is characterized in that: the sidewall of described tank body offers blowdown oilhole near tank body middle and lower part, described blowdown oilhole is communicated with blowdown fuel tap (104); Described upper cover is dome head, and low head is dome head or conical end socket; Described upper cover upper end is also provided with Pressure gauge and thermometer; Described low head offers limber hole near discharge outlet, and described limber hole is communicated with blowdown water valve (110).
4. changing food waste hydrolysis process device more than kitchen according to claim 3, is characterized in that: the bottom of described warehouse (502) near the side of described hinge (507d) higher than the side near described drainage conduit (501); The bottom of described warehouse (502) offers the sewage collecting ditch (511) with described horizontal conveyer (504) axis being parallel near the side of described drainage conduit (501); The bottom of described warehouse (502) below horizontal striker plate offers T-shaped foundation ditch (506), described T-shaped foundation ditch (506) width is greater than the width of described longitudinal conveyer (508) and horizontal conveyer (504), and described longitudinal conveyer (508) and horizontal conveyer (504) are arranged in described T-shaped foundation ditch (506).
5. changing food waste hydrolysis process device more than kitchen according to claim 4, it is characterized in that: in the T-shaped foundation ditch (506) of described horizontal striker plate (509) below, be provided with receiving hopper (510), the discharging opening of described receiving hopper (510) lower end is positioned at described horizontal conveyer (504) top, and described longitudinal conveyer (508) stretches into the top of described receiving hopper (510) near described horizontal conveyer (504) one end.
6. changing food waste hydrolysis process device more than kitchen according to claim 5, is characterized in that: described warehouse (502) offers door (503) near described drainage conduit (501) place.
7. changing food waste hydrolysis process device more than kitchen according to claim 6, is characterized in that: face upward and be 5-15 ° with horizontal plane angle in described drainage conduit (501) discharge direction.
8. changing food waste hydrolysis process device more than kitchen according to claim 7, is characterized in that, the quick-fried off-load storehouse of described spray leads system by armored concrete to form, volume position 500-2000m
3, can bear the surge of 0.4-0.5Mpa, the pressure of hot dry wind air accumulator bears as 0.1-0.6Mpa.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520773304.1U CN205110337U (en) | 2015-09-30 | 2015-09-30 | Surplus kitchen garbage in kitchen processing apparatus that hydrolysises |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520773304.1U CN205110337U (en) | 2015-09-30 | 2015-09-30 | Surplus kitchen garbage in kitchen processing apparatus that hydrolysises |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205110337U true CN205110337U (en) | 2016-03-30 |
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ID=55565985
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520773304.1U Expired - Fee Related CN205110337U (en) | 2015-09-30 | 2015-09-30 | Surplus kitchen garbage in kitchen processing apparatus that hydrolysises |
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| CN (1) | CN205110337U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105080943A (en) * | 2015-09-30 | 2015-11-25 | 宜兴合一环保科技有限公司 | Kitchen and food waste hydrolysis treatment device and treatment technology thereof |
-
2015
- 2015-09-30 CN CN201520773304.1U patent/CN205110337U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105080943A (en) * | 2015-09-30 | 2015-11-25 | 宜兴合一环保科技有限公司 | Kitchen and food waste hydrolysis treatment device and treatment technology thereof |
| CN105080943B (en) * | 2015-09-30 | 2017-06-06 | 宜兴合一环保科技有限公司 | A kind of food waste kitchen garbage hydrolysis process device and its handling process |
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