CN202322431U - Oil separation recycle device of kitchen wastes - Google Patents

Oil separation recycle device of kitchen wastes Download PDF

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Publication number
CN202322431U
CN202322431U CN2011204826652U CN201120482665U CN202322431U CN 202322431 U CN202322431 U CN 202322431U CN 2011204826652 U CN2011204826652 U CN 2011204826652U CN 201120482665 U CN201120482665 U CN 201120482665U CN 202322431 U CN202322431 U CN 202322431U
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CN
China
Prior art keywords
tank body
separating
reclaiming device
oil
strainer
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
CN2011204826652U
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Chinese (zh)
Inventor
谢非
陈科宇
金涛
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Deepblue Environmental Protection Technologies Co., Ltd.
Original Assignee
SICHUAN DEEPBLUE ENVIRONMENTAL TECHNOLOGIES Co Ltd
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Publication date
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Priority to CN2011204826652U priority Critical patent/CN202322431U/en
Application granted granted Critical
Publication of CN202322431U publication Critical patent/CN202322431U/en
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Abstract

The utility model provides an oil separation recycle device of kitchen wastes for processing slurries of kitchen wastes obtained after thermal hydrolysis reaction. The recycle device comprises a jar which uses a hydro-cyclone separation structure to enable slurries to rotate along the feed jetting direction; and a filter for gathering an oil phase is arranged on the top of the jar. The oil separation recycle device is based on the hydro-cyclone separation, and has the advantages of air floatation oil removing, feeding oil removing, capabilities of improving the oil recycle rate and the oil purity.

Description

A kind of grease separating and reclaiming device of diet and kitchen wastes
Technical field
The utility model relates to a kind of surplus rubbish of meal that is directed against and extracts greasy tripping device, and particularly a kind of diet and kitchen wastes that is directed against after thermal hydrolysis is handled reclaims greasy device.
Background technology
Along with the high speed development of Chinese national economy, living standards of the people improve day by day, and the output of rubbish from cooking also increases day by day, brings huge environmental stress to the city.High fat content in the changing food waste makes it in disposal process, has many hidden danger.For example, oil fermentation very easily produces carcinogenic substance---flavacin, and harm humans is healthy; In the rubbish biological treatment process, because of grease can wrap up Supporting Media, and disturb the microbial life activity, influence treatment effect; Because of grease adheres to pipeline, wall, and cause line clogging easily.Thereby,, changing food waste need remove grease usually in handling.Waste oil in the changing food waste is again ideal bio oil fuel and daily-use chemical industry raw material, can recycling.A kind of changing food waste water-and-oil separator is disclosed among the Chinese patent CN201445853U; This equipment comprises water-and-oil separator and rotary squeezer; Changing food waste promotes and presses under the extruding of cage at the screw-blade of rotary squeezer, and moisture and grease contained in the rubbish are squeezed out.Waste residue after the press for extracting juice is discharged through discharge port, and the expressed oil-water mixture flows to strumbox through liquid collecting plate with the following conduit that is connected, and strumbox is with the solid granule elimination further of mixed solution, and the profit after the filtration flows to water separation tank.Water separation tank is the communicating vessels shape, be the basis with the gravity type boat davit separation principle, is core with the coarse method, and oil and water sepn are come.This equipment deficiency is to squeeze insufficient, and grease can not fully be separated out and filter and extract, and the recovery is low.
The utility model content
In order to solve the not high problem of the grease recovery in the prior art, the utility model provides a kind of and carries out the greasy retrieving arrangement of high efficiente callback to the diet and kitchen wastes after the thermal hydrolysis processing.
For realizing above-mentioned purpose, the technical scheme that the utility model provides is following:
A kind of diet and kitchen wastes grease separating and reclaiming device, the slurry of the diet and kitchen wastes that obtains after the reaction of processing thermal hydrolysis comprises tank body, said tank body adopts the hydrocyclone isolating construction, so that the direction rotation that slurry sprays along charging; The top of said tank body is provided with the strainer that is used for enrichment grease phase.
Further, said tank body is divided into four WSs; First WS is the grease phase region that is positioned at part on the strainer; The secondary service area is near the rotational flow separation district of opening for feed that is positioned at said tank body; The 3rd WS is the water district that is positioned at the lower middle portion of said tank body, and the 4th WS is the liquid-solid mixing phase region that is positioned at the bottom of said tank body.
Further, the strainer of said tank body adopts the plastic optical fibre filler.
Preferably, the coarse grain plastic optical fibre material of said strainer employing oleophilic drainage character is as filler.
Further, the below of the opening for feed of said tank body is provided with and is used to feed compressed-air actuated aeration opening.
Further, said aeration opening is provided with micro porous aeration head.
Further, the below of the aeration opening of said tank body sets out the mouth of a river.
Further, the top of said tank body is provided with oil outlet; The bottom of said tank body is provided with the discharge port that concentrates slurry.
The technique effect of the utility model:
1, this use is novel is a kind of mechanical type separating device of static state, adopts the mode of hydrocyclone to carry out oil, water, solid separation.Disengaging time is short, and running cost is low; Need not to add any medicament, recoil or change internals, and work is continuous, automatic, stable, have the characteristic of wide operating restraint.
2, this uses the novel appts volume little, and floor space is little, and is pollution-free, convenient operating maintenance, and equipment cost is low.
3, this utility model is the basis with the rotational flow separation, has the advantage of oil removal by air bubbling, filler oil removing concurrently, can improve the grease recovery, and can improve grease purity.
Description of drawings
Fig. 1 is the structural representation of the utility model.
Among the figure, 1, tank body 2, opening for feed 3, discharge port 4, water outlet 5, aeration opening 6, oil outlet 7, strainer 8, supporting leg.
Embodiment
Combine accompanying drawing that the technical scheme of the utility model is elaborated in this part.
Can know that as those skilled in the art the kinetic viscosity of the rubbish from cooking after the thermal hydrolysis art breading reduces greatly, be about 100~1000CP, better mobile.According to these characteristics, the isolating working mechanism of the utility model employing waterpower spinning liquid carries out profit to be separated admittedly, to reclaim grease.
Fig. 1 has shown an instance of the utility model Separation and Recovery equipment.The main body of Separation and Recovery device is a tank body 1, and this tank body 1 is designed to cyclone separator.The top of tank body 1 is provided with oil outlet 6; The middle and upper part is provided with opening for feed 3, and the top of this opening for feed 3 is provided with strainer 7, and the below is provided with and is used to feed compressed-air actuated aeration opening 5; The below of aeration opening 5 sets out the mouth of a river 4, and the bottom of tank body 1 is provided with the discharge port 2 that concentrates slurry.Above-mentioned aeration opening is provided with micro porous aeration head, and the prior art capable of using that is provided with owing to micro porous aeration head does not have depicted in greater detail for this reason in the drawings, no longer specifies yet.Scrutable as those skilled in the art, above-mentioned strainer 7 can adopt any filtration and material of being used in the prior art, also comprises the filler shown in the present embodiment.Also be provided with leg 8 on the tank body, to be used for fixing support.
The inside of whole tank body 1 is divided into four layers, and top (on the strainer 7) is the grease phase region, and middle part (near the opening for feed 2) is the rotational flow separation district, and lower middle portion is the water district, and the bottom is liquid-solid mixing phase region.Because the Field Characteristics of above-mentioned Separation and Recovery device mainly shows the free vortex that is as the criterion, and except the centrifugal settling effect, strengthens coalescence and adsorption process in addition, thereby strengthens the effect of settlement separate process.The coarse plastic optical fibre material that in tank body 1 top oil phase, is provided with oleophilic drainage character as the grease enriching apparatus, can improve greasy purity as filler.
When the Separation and Recovery device moved, the surplus slurry in the kitchen after the hydro-thermal injected in the cyclone separator 1 from opening for feed 2 with certain pressure, speed, produces centrifuge field; Drive the direction rotation that the slurry in the tank body 1 sprays along charging; Because water, solid density are bigger than greasy, the little grease of density is brought to the whirlpool middle part mutually and moves upward, through the further enrichment of the plastic optical fibre filler in the strainer 7; Oil outlet 6 overflows are discharged from the top at last; The water of telling is discharged from the water outlet 4 of middle and lower part continuously, and spissated slurry is deposited on chamber, the end, discharges from bottom discharge mouth 3.Simultaneously, aeration opening 5 can feed pressurized air, and through micro porous aeration head, forms the less bubble of diameter, drives less grease motion, the collision of particle diameter in the disengaging zone, and is final floating to oil phase, can further improve the grease recovery.
It should be noted that; The above is merely the preferred embodiment of the utility model; Be not so limit the scope of patent protection of the utility model, the utility model can also carry out the improvement of material and structure to the structure of above-mentioned various component, or employing technical equivalents thing is replaced.So the specification sheets of all utilization the utility model and the equivalent structure that diagramatic content is done change, or directly or indirectly apply to other correlative technology fields and all in like manner all be contained in the scope that the utility model contains.

Claims (8)

1. diet and kitchen wastes grease separating and reclaiming device is handled the slurry of the diet and kitchen wastes that obtains after the thermal hydrolysis reaction, it is characterized in that comprise tank body, said tank body adopts the hydrocyclone isolating construction, so that the direction rotation that slurry sprays along charging; The top of said tank body is provided with the strainer that is used for enrichment grease phase.
2. separating and reclaiming device according to claim 1 is characterized in that, said tank body is divided into four WSs; First WS is the grease phase region that is positioned at part on the strainer; The secondary service area is near the rotational flow separation district of opening for feed that is positioned at said tank body; The 3rd WS is the water district that is positioned at the lower middle portion of said tank body, and the 4th WS is the liquid-solid mixing phase region that is positioned at the bottom of said tank body.
3. separating and reclaiming device according to claim 2 is characterized in that, the strainer of said tank body adopts the plastic optical fibre filler.
4. separating and reclaiming device according to claim 3 is characterized in that, the strainer of said tank body with the coarse grain plastic optical fibre material of oleophilic drainage character as filler.
5. according to arbitrary described separating and reclaiming device among the claim 1-4, it is characterized in that the below of the opening for feed of said tank body is provided with and is used to feed compressed-air actuated aeration opening.
6. separating and reclaiming device according to claim 5 is characterized in that said aeration opening is provided with micro porous aeration head.
7. separating and reclaiming device according to claim 6 is characterized in that the below of the aeration opening of said tank body sets out the mouth of a river.
8. separating and reclaiming device according to claim 7 is characterized in that the top of said tank body is provided with oil outlet; The bottom of said tank body is provided with the discharge port that concentrates slurry.
CN2011204826652U 2011-11-29 2011-11-29 Oil separation recycle device of kitchen wastes Expired - Lifetime CN202322431U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011204826652U CN202322431U (en) 2011-11-29 2011-11-29 Oil separation recycle device of kitchen wastes

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011204826652U CN202322431U (en) 2011-11-29 2011-11-29 Oil separation recycle device of kitchen wastes

Publications (1)

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CN202322431U true CN202322431U (en) 2012-07-11

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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103214152A (en) * 2013-05-10 2013-07-24 陈卫国 Waste liquid regeneration machine
WO2014079170A1 (en) * 2012-11-23 2014-05-30 华南再生资源(中山)有限公司 Distillation-free biodiesel production method and system
CN103977628A (en) * 2014-03-26 2014-08-13 嘉兴市绿能废弃油脂回收有限公司 Separation method for oil-water slag generated during refining of swill-cooked dirty oil
CN105694999A (en) * 2016-04-27 2016-06-22 唐山金利海生物柴油股份有限公司 High-quality low-sulfur-content biodiesel production equipment and technology
CN105750305A (en) * 2016-04-11 2016-07-13 深圳市瑞赛尔环保设备有限公司 Pre-treatment device of grease of kitchen wastes
CN106673091A (en) * 2017-02-24 2017-05-17 湖北君集水处理有限公司 Cyclone separator of straight tube effluent structure
CN106698553A (en) * 2017-02-24 2017-05-24 湖北君集水处理有限公司 Cyclone separator with U-shaped pipe water outlet structure
CN107050994A (en) * 2017-02-24 2017-08-18 湖北君集水处理有限公司 The cyclone separator of water water flowing out structure is received in a kind of combination
CN108261879A (en) * 2018-03-05 2018-07-10 上海成东科技有限公司 Supercritical CO2The buffering filter of extraction equipment

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014079170A1 (en) * 2012-11-23 2014-05-30 华南再生资源(中山)有限公司 Distillation-free biodiesel production method and system
CN103214152A (en) * 2013-05-10 2013-07-24 陈卫国 Waste liquid regeneration machine
CN103977628A (en) * 2014-03-26 2014-08-13 嘉兴市绿能废弃油脂回收有限公司 Separation method for oil-water slag generated during refining of swill-cooked dirty oil
CN103977628B (en) * 2014-03-26 2016-02-10 嘉兴市绿能废弃油脂回收有限公司 The separation method of oil-water residue in a kind of waste oil extractive process
CN105750305A (en) * 2016-04-11 2016-07-13 深圳市瑞赛尔环保设备有限公司 Pre-treatment device of grease of kitchen wastes
CN105750305B (en) * 2016-04-11 2018-07-17 深圳市瑞赛尔环保设备有限公司 Kitchen garbage grease pretreatment unit
CN105694999A (en) * 2016-04-27 2016-06-22 唐山金利海生物柴油股份有限公司 High-quality low-sulfur-content biodiesel production equipment and technology
CN105694999B (en) * 2016-04-27 2017-05-17 唐山金利海生物柴油股份有限公司 High-quality low-sulfur-content biodiesel production equipment and technology
CN106673091A (en) * 2017-02-24 2017-05-17 湖北君集水处理有限公司 Cyclone separator of straight tube effluent structure
CN106698553A (en) * 2017-02-24 2017-05-24 湖北君集水处理有限公司 Cyclone separator with U-shaped pipe water outlet structure
CN107050994A (en) * 2017-02-24 2017-08-18 湖北君集水处理有限公司 The cyclone separator of water water flowing out structure is received in a kind of combination
CN108261879A (en) * 2018-03-05 2018-07-10 上海成东科技有限公司 Supercritical CO2The buffering filter of extraction equipment

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C14 Grant of patent or utility model
GR01 Patent grant
C56 Change in the name or address of the patentee
CP01 Change in the name or title of a patent holder

Address after: 216, room 7, building 1480, hi tech incubator Park, north section of Tianfu Road, Chengdu hi tech Zone, Sichuan, 610042

Patentee after: Deepblue Environmental Protection Technologies Co., Ltd.

Address before: 216, room 7, building 1480, hi tech incubator Park, north section of Tianfu Road, Chengdu hi tech Zone, Sichuan, 610042

Patentee before: Sichuan Deepblue Environmental Technologies Co., Ltd.

CP02 Change in the address of a patent holder

Address after: 610042 Sichuan China (Sichuan) free trade test zone, Chengdu hi tech Zone, 8, three Tai 1, new hope international 1, unit 24 (1-8)

Patentee after: Deepblue Environmental Protection Technologies Co., Ltd.

Address before: 216, room 7, building 1480, hi tech incubator Park, north section of Tianfu Road, Chengdu hi tech Zone, Sichuan, 610042

Patentee before: Deepblue Environmental Protection Technologies Co., Ltd.

CP02 Change in the address of a patent holder
CX01 Expiry of patent term

Granted publication date: 20120711

CX01 Expiry of patent term