CN106145513A - A kind of equipment for treating dining garbage - Google Patents
A kind of equipment for treating dining garbage Download PDFInfo
- Publication number
- CN106145513A CN106145513A CN201510176084.9A CN201510176084A CN106145513A CN 106145513 A CN106145513 A CN 106145513A CN 201510176084 A CN201510176084 A CN 201510176084A CN 106145513 A CN106145513 A CN 106145513A
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- China
- Prior art keywords
- equipment
- reactive tank
- centralized collection
- dining garbage
- treating dining
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- Water Treatment By Sorption (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention discloses a kind of equipment for treating dining garbage; by food and drink waste water respectively by the finly filtration net of coarse filtration net, 0.025~0.5mm that string diameter is 1~0.5mm, filtered through gauze net filtration; the thorough solid-liquid separation of food debris and waste water is made to come; the solid waste being filtrated to get is by stirring, pulverize, grind thoroughly granulating; then food debris is made to hydrolyze by torulopsis bacterium; remove the float in refuse, colloid and organic eventually through electrodeless biological adsorption oxidative degradation groove, waste water is finally discharged by the discharge outlet of reactive tank.Elimination efficiency of the present invention is good, and non-secondary pollution, and investment cost is low, is worthy to be popularized.
Description
Technical field
The present invention relates to the processing means of a kind of rubbish, be specifically related to a kind of equipment for treating dining garbage.
Background technology
Food garbage refers to the undressed waste water discharged by catering trade, has been characterized in substantial amounts of food debris, colloidal particle and float, has been mainly composed of animal and plant fat, detergent and protein etc..These food debriss as processed not in time, after being allowed to be discharged into rivers,lakes and seas, can make water turbidity, can make rivers and lakes water blackening, and give out foul smell during summer, drastically influence the healthy of natural environment and people.
At present, under the food debris in food and drink waste water is by filtering, then solid waste is filled, secondary operations, the illegal unscrupulous merchant etc. making waste oil has an opportunity to take advantage of, have a strong impact on the health of human body, and wasted human and material resources, even environment can be produced secondary pollution.
Summary of the invention
The invention reside in and solve the technical problem that in food and drink waste water, food debris removing is not in place, the minimizing technology of food debris in a kind of efficient food and drink waste water is provided, by three filtrations, attrition grinding, biological adsorption oxidative degradation, food debris is made thoroughly to hydrolyze, it is achieved the very removal of food debris thing.
For solving above-mentioned technical problem, the present invention adopts the following technical scheme that
A kind of equipment for treating dining garbage, including coarse filtration net, finly filtration net, filtered through gauze net, centralized collection district, stirring reducing mechanism and grinder, reaction unit, described coarse filtration net, finly filtration net, filtered through gauze Netcom cross connecting gear and connect, and be all connected with described centralized collection district;Described stirring reducing mechanism is arranged in described centralized collection district, connects thereafter described grinder, and described reaction unit connects described grinder.
Further, being added with additive in described reaction unit, described additives ratio is pressed per kilogram abrasive material and is added 3~4kg water, 0.01~0.02kg methanol, 0.03~0.06kg sodium bicarbonate, 0.002~0.005kg torulopsis bacterium.
Further, described centralized collection district is provided with baffle, and baffle divides into one, 2 two parts described centralized collection, and described stirring reducing mechanism is arranged in centralized collection district one.
Further, in described grinder is arranged at described centralized collection district two.
Further, described reaction unit includes high-speed stirring apparatus, gas skirt, and reactive tank, and described reactive tank connects described high-speed stirring apparatus.
Further, described reactive tank is divided into filtration fraction and absorption degradation two parts.
Further, described reactive tank filtration fraction includes that first order suspended particulate substance reactive tank is the screen cloth of ceramic sintering;Second level suspended particulate substance reactive tank is the screen cloth that brucite is fired;Third level floating particles thing reactive tank is the screen cloth that attapulgite is fired.
Further, described fourth stage colloid adsorption tank is the adsorption tank that the intercalation soil of spray is filled;Level V oxidation trough 5 is electrolytic oxidation groove.
The present invention compared with prior art, has the advantages that employing is added torulopsis bacterium and carried out a biological disposal upon through hot fermentation so that food debris is degradable, compared with traditional landfill, processing method, it is to avoid pollution and the waste of resource to environment;By Pyatyi biological adsorption oxidative degradation groove progressively to different-grain diameter in the liquid mixing material after converting
Material carry out staged care, substantially increase after conversion the removal efficiency of COD material in liquid mixture.
Accompanying drawing explanation
Fig. 1 is the process chart of the present invention.
1-coarse filtration net;2-finly filtration net;3-filtered through gauze net;4-centralized collection district;5-stirs reducing mechanism;6-grinder;7-reaction unit;71-high-speed stirring apparatus;72-gas skirt 8;73-reactive tank;;731-suspended particulate substance reactive tank;732-suspended particulate substance reactive tank;12-suspended particle thing reactive tank 3;734-colloid adsorption tank;735-oxidation trough.
Detailed description of the invention
In order to make those of ordinary skill in the art more understand the object, technical solutions and advantages of the present invention, below in conjunction with drawings and Examples, the present invention is further elaborated.
As it can be seen, the minimizing technology of food debris in a kind of food and drink waste water, a kind of equipment for treating dining garbage, its step processing rubbish is as follows:
Step 1: first by food and drink waste water respectively by coarse filtration net 1, finly filtration net 2, filtered through gauze net 3 realizes the solid-liquid separation of food and drink;
Step 2: the solid waste that solid-liquid separation obtains enters centralized collection district 4, thoroughly pulverize subsequently in stirring reducing mechanism 5, food debris after thoroughly pulverizing enters grinder 6 and is fully ground, and presses per kilogram abrasive material and add 3~4kg water, 0.01~0.02kg methanol, 0.03~0.06kg sodium bicarbonate, 0.002~0.005kg after grinding
Torulopsis bacterium, and carry out the regulation of pH, the pH making mixture is 6.3 ~ 7.5;
Step 3: said mixture matter enters heated at high speed agitating device 71 and heats so that it is temperature is maintained at 38 ° of C~53 ° of C, and high-speed stirred 12~24 hours, the gas gas skirt 72 of generation is collected;
Step 4: the mixture after high-speed stirred enters reactive tank 73, waste water is finally discharged by the outlet of reactive tank.
Coarse filtration net uses string diameter 1~0.5mm, mesh number is 4~600 mesh, and finly filtration net 2 uses string diameter to be 0.025~0.5mm;Torulopsis bacterium, it is by Fructus Hordei Germinatus inclined-plane amplification culture, then obtains surface ruffle, the bacterium colony of matt neat in edge through screening;Pyatyi biological adsorption oxidative degradation groove 9 first order is 80~150um suspended particulate substance reactive tanks for removing particle diameter);The second level is 60~80um suspended particulate substance reactive tanks for removing particle diameter);The third level is 40~60 floating particles thing reactive tanks for removing particle diameter;The fourth stage is 1~20nm colloid adsorption tank for removing particle diameter;Level V is for removing dissolubility organic oxidation groove.
Claims (8)
1. an equipment for treating dining garbage, including coarse filtration net (1), finly filtration net (2), filtered through gauze net (3), centralized collection district (4), stirring reducing mechanism (5) and grinder (6), reaction unit (7), it is characterized in that: described coarse filtration net (1), finly filtration net (2), filtered through gauze net (3) connect (8) by connecting gear, and be all connected with described centralized collection district (4);Described stirring reducing mechanism (5) is arranged in described centralized collection district (4), connects thereafter described grinder (6), and described reaction unit (7) connects described grinder (6).
Equipment for treating dining garbage the most according to claim 1, it is characterized in that: be added with additive in described reaction unit (7), described additives ratio is pressed per kilogram abrasive material and is added 3~4kg water, 0.01~0.02kg methanol, 0.03~0.06kg sodium bicarbonate, 0.002~0.005kg torulopsis bacterium.
Equipment for treating dining garbage the most according to claim 1, it is characterized in that: described centralized collection district (4) is provided with baffle (41), baffle (41) divides into one (42), two (43) two parts described centralized collection, and described stirring reducing mechanism (5) is arranged in centralized collection district one (42).
Equipment for treating dining garbage the most according to claim 3, it is characterised in that: described grinder (6) is arranged in described centralized collection district two (43).
5. according to the equipment for treating dining garbage described in Claims 1-4 any claim, it is characterized in that: described reaction unit (7) includes high-speed stirring apparatus (71), gas skirt (72), and reactive tank (73), described reactive tank (73) connects described high-speed stirring apparatus (71).
Equipment for treating dining garbage the most according to claim 5, it is characterised in that: described reactive tank (73) is divided into filtration fraction and absorption degradation two parts.
Equipment for treating dining garbage the most according to claim 6, it is characterised in that: described reactive tank filtration fraction includes that first order suspended particulate substance reactive tank (731) is the screen cloth of ceramic sintering;Second level suspended particulate substance reactive tank (732) is the screen cloth that brucite is fired;Third level floating particles thing reactive tank (733) is the screen cloth that attapulgite is fired.
Equipment for treating dining garbage the most according to claim 6, it is characterised in that: fourth stage colloid adsorption tank (734) is the adsorption tank that the intercalation soil of spray is filled;Level V oxidation trough (735) is electrolytic oxidation groove, by the deliquescent organic substance of electrolytic oxidation.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510176084.9A CN106145513A (en) | 2015-04-15 | 2015-04-15 | A kind of equipment for treating dining garbage |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510176084.9A CN106145513A (en) | 2015-04-15 | 2015-04-15 | A kind of equipment for treating dining garbage |
Publications (1)
Publication Number | Publication Date |
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CN106145513A true CN106145513A (en) | 2016-11-23 |
Family
ID=57336109
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201510176084.9A Pending CN106145513A (en) | 2015-04-15 | 2015-04-15 | A kind of equipment for treating dining garbage |
Country Status (1)
Country | Link |
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CN (1) | CN106145513A (en) |
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2015
- 2015-04-15 CN CN201510176084.9A patent/CN106145513A/en active Pending
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Application publication date: 20161123 |