CN206240916U - A kind of oil-containing material high carries oil system - Google Patents

A kind of oil-containing material high carries oil system Download PDF

Info

Publication number
CN206240916U
CN206240916U CN201621179322.8U CN201621179322U CN206240916U CN 206240916 U CN206240916 U CN 206240916U CN 201621179322 U CN201621179322 U CN 201621179322U CN 206240916 U CN206240916 U CN 206240916U
Authority
CN
China
Prior art keywords
oil
squeezer
tank
discharging opening
wet solution
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.)
Active
Application number
CN201621179322.8U
Other languages
Chinese (zh)
Inventor
高源�
张峰
孙树群
张雷
杜静
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.)
Weide Environment Technology Co Ltd
Original Assignee
Weide Environment Technology Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Weide Environment Technology Co Ltd filed Critical Weide Environment Technology Co Ltd
Priority to CN201621179322.8U priority Critical patent/CN206240916U/en
Application granted granted Critical
Publication of CN206240916U publication Critical patent/CN206240916U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Treatment Of Sludge (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

Oil system is carried the utility model discloses a kind of oil-containing material high, the utility model is related to oily material processing technology field.The utility model includes wet solution tank, pressure surge tank, thickness squeezer and oil-water separation system, is connected by the delivery pump on conveyance conduit between each several part.The thickness squeezer includes thick squeezer, gravity riffler and thin squeezer, and the oil-water separation system includes mixed liquor tank diameter, three-phase separator and attached tank body.Out, the inorganic matter for making density larger is easier to settle, separates separation of animal and vegetable oils of the kitchen garbage in material is incorporated under wet solution is acted on, and the organic matter in material is dissolved, fiber is refined, and reduces material viscosity coefficient.Three-phase separator is re-fed into by feed separation into oil, water, the part of slag three, material is decomposed and is maximized, impurity-eliminating effect is improved, water-oil separating is more thorough, carrying oil system oil extracting rate than tradition improves 3%.

Description

A kind of oil-containing material high carries oil system
Technical field
The utility model is related to oily material processing technology field.
Background technology
At present, kitchen garbage increasingly manifests to the pollution of environment and the harm of public health security, the harm of kitchen garbage The great attention of civic strong interest and municipal government is caused.Most of main processing means of kitchen garbage have following several:
1. penkeeping is used directly to, serious " rubbish pig " phenomenon is caused;
2. waste oil is processed into by illegal retailer and is sold to food and beverage enterprise, be detrimental to health;
3. kitchen garbage is arbitrarily abandoned, and severe contamination is caused to urban environment;
4. house refuse into MSW Incineration Plant burning disposal is mixed into.
This behavior serious harm public food is safe and healthy.In order to scientifically and rationally utilize these waste greases, have Kitchen waste grease is processed further purification and is made low grade by enterprise by regular legal channel using advanced handling process The handicraft product such as industrial oleic acid, stearic acid and commercial grease, non-phosphide detergent and biodiesel (fatty acid methyl ester), realize The harmless treatment of kitchen waste grease and recycling.
The core system that oil system is kitchen garbage pretreatment and water-oil separating is put forward, is the weight of waste grease recycling The operations such as treatment process, removal of impurities, water-oil separating in kitchen waste grease pretreatment process are wanted, is generally at present artificial operation, it is general Environment is poor at the scene, labour intensity is high, impurity-eliminating effect is bad for store-through, water-oil separating not thoroughly, efficiency is low, the rate of recovery is low lacks Point.
Utility model content
The technical problems to be solved in the utility model is directed to above-mentioned the deficiencies in the prior art, there is provided a kind of oil-containing material high Oil system is carried, oil-containing material high is solved and is processed unscientific problem, so as to reach oily material integrated treatment, improved effect, reduce The purpose of environmental pollution.
In order to solve the above technical problems, technical solution adopted in the utility model is:A kind of oil-containing material high carries oily system System includes wet solution tank, pressure surge tank, thickness squeezer and oil-water separation system, between the wet solution tank and pressure surge tank Delivery pump one is connected with conveyance conduit, conveying is connected with the conveyance conduit between the pressure surge tank and thickness squeezer Pump two, delivery pump three is connected with the conveyance conduit between the thickness squeezer and oil-water separation system;
The thickness squeezer includes:Thick squeezer, gravity riffler and thin squeezer, the thick squeezer material charging Mouth is connected with the pressure surge tank discharging opening, and thick squeezer material squeezes discharging opening and the gravity riffler charging aperture phase Even, the gravity riffler discharging opening is connected with the thin squeezing machine inlet, the thin squeezer discharging opening and water-oil separating Mixed liquor tank diameter in system is connected by pipeline;
The oil-water separation system includes mixed liquor tank diameter, three-phase separator and attached tank body, the mixed liquor stirring Being connected between groove and three-phase separator makes the impeller pump of the inlet amount stabilization of three-phase separator, the impeller pump use frequency conversion control System.
Preferably, the wet solution tank uses steam direct heating, and the wet solution tank includes automatic control system, automatically controls System is automatically controlled to the temperature in course of reaction, pressure, liquid level and heat time.
Preferably, the thick squeezer discharging opening includes squeezing discharging opening and impurity discharging opening, and the thick squeezer can be by Impurity in material more than 12mm is separated, and carries out mechanical expression dehydration to impurity, and the impurity after squeezing is gone out by impurity Material mouth is delivered to by enclosed belt conveyor and transhipment is stored between debris accumulating.
Preferably, the gravity riffler also includes sand setting mechanism, and the sand setting mechanism is arranged in cell body, by gravity Settlement action settles the heavy gravel in material.
It is using the beneficial effect produced by above-mentioned technical proposal:The oil-containing material high carries oil system, including wet solution tank, Pressure surge tank, thickness squeezer and oil-water separation system, wet solution tank carry out wet solution treatment, kitchen under given temperature and pressure Vegetable and animals oils during rubbish is incorporated into material under the effect of wet solution are sufficiently separated out, while reducing material viscosity, make density Larger inorganic matter is easier to settle, separates, and the organic matter in material is dissolved, fiber is refined, and makes material viscosity coefficient Reduce, possess good mobility.Pressure surge tank has makes material be cached in pressure surge tank, the work of pressure release and cooling With, it is ensured that it is smoothed out in follow-up work.Thickness squeezer can by the impurity in material after wet solution carry out mechanical expression dehydration, The sedimentation of heavy gravel and the abjection of long fibre organic matter, are re-fed into three-phase separator by feed separation into oil, water, slag three Point, resource is made full use of, decompose material and maximize, impurity-eliminating effect is improved, water-oil separating is more thorough, in hgher efficiency, the rate of recovery Lifting, carries oil system oil extracting rate and improves 3% than tradition.
Brief description of the drawings
Fig. 1 is the operation principle schematic diagram of the utility model embodiment.
In figure:1st, wet solution tank;11st, wet solution tank charging aperture;12nd, wet solution tank discharging opening;2nd, pressure surge tank;21st, pressure delays Rush tank charging aperture;22nd, pressure surge tank discharging opening;3rd, thickness squeezer;31st, thick squeezer;311st, machine inlet is slightly squeezed; 312nd, thick squeezer squeezing discharging opening;32nd, gravity riffler;321st, gravity riffler charging aperture;322nd, gravity riffler discharging Mouthful;33rd, thin squeezer;331st, machine inlet is carefully squeezed;332nd, thin squeezer discharging opening;4th, oil-water separation system;41st, mixed liquor Tank diameter;42nd, three-phase separator;5th, delivery pump one;6th, delivery pump two;7th, delivery pump three.
Specific embodiment
The utility model is described in further detail with reference to the accompanying drawings and detailed description.
As shown in figure 1, putting forward the operation principle schematic diagram of oil system for a kind of oil-containing material high of the utility model.The system bag Wet solution tank 1, pressure surge tank 2, thickness squeezer 3 and oil-water separation system 4 are included, it is defeated between wet solution tank 1 and pressure surge tank 2 Send and be connected with pipeline delivery pump 1, delivery pump is connected with the conveyance conduit between pressure surge tank 2 and thickness squeezer 3 26, delivery pump 37 is connected with the conveyance conduit between thickness squeezer 3 and oil-water separation system 4.
Wet solution treatment is that kitchen garbage is carried out wet solution treatment under the conditions of certain temperature and pressure.Kitchen garbage is made in wet solution The vegetable and animals oils being incorporated under in material are sufficiently separated out, while reducing material viscosity, make the inorganic matter that density is larger Easily settle, separate, and the organic matter in material is dissolved, fiber is refined, material viscosity coefficient reduces, and possesses good Mobility.The wet solution design pressure 0.6MPa of tank 1, using steam direct heating, the working reaction temperature of wet solution tank 1 is 90~130 DEG C, working reaction pressure is 0.3~0.4 MPa, and the reaction time is between 30min~180min.The steam inlet one of wet solution tank 1 Respectively in the top and bottom of tank body and vertically opposite with steam inlet two, steam inlet one is with steam inlet two respectively from tank Body top and bottom collective effect, makes steam quickly fill with tank body, is sufficiently mixed with kitchen garbage, makes wet solution reaction more abundant. Automatic control system in filling is automatically controlled to the temperature in course of reaction, pressure, liquid level and heat time.Pressure buffer The design pressure of tank 2 is 0.4MPa, and volume is 20m3.After the wet solution of material, by wet solution tank 1 by pressure-feed mode discharge to pressure Power surge tank 2, material is cached in pressure surge tank 2, pressure release, to be subsequent discharged into and carry out squeezing sorting in thickness squeezer 3.
Thickness squeezer 3 includes:Thick squeezer 31, gravity riffler 32 and thin squeezer 33, thick squeezer material charging Mouth 311 is connected with pressure surge tank discharging opening 22, and thick squeezer material squeezes discharging opening 312 and gravity riffler charging aperture 321 It is connected, the gravity riffler discharging opening 322 is connected with thin squeezing machine inlet 331, and thin squeezer discharging opening 332 divides with profit Mixed liquor tank diameter 41 in system 4 is connected by pipeline, the oily material of the transmission of delivery pump 37.
The function of thick squeezer 31 is to sub-elect the impurity in material more than 12mm, and mechanical expression is carried out to impurity takes off Water, reduces the loss of organic materials.By storing up between the impurity after press dewatering is delivered to debris accumulating by enclosed belt conveyor Deposit transhipment.Gravity riffler 32 stores and sand setting mechanism is set in the filtrate being press-filtered out by thick squeezer 31, cell body, heavy by gravity Drop effect settles the heavy gravel in material, artificial periodically to remove.Contain a large amount of long fibre organic matters in filtrate after wet solution, lead to This part long fibre organic matter squeezing abjection is together carried out Composting treatment by meticulous squeezer 33 after collection with anaerobism biogas residue. In importing mixed liquor tank diameter 41 by pipeline by delivery pump 37 through the filtrate after meticulous squeezer 33, carried out after homogeneous oil, Water, slag three phase separation.
The major function of oil-water separation system is that oil, water, slag three phase separation are carried out to organic slurry, oil-water separation system by Mixed liquor tank diameter 41, three-phase separator 42 and attached tank body composition.
Material is stirred in mixed liquor tank diameter 41 first, then uniformly sends into three phase separation by impeller pump Machine 42 carries out water-oil separating.Impeller pump uses VFC, it is ensured that the inlet amount stabilization of three-phase separator 42.
Three-phase separator 42 is by feed separation into oil, water, the wherein part of slag three, oil phase(Industrial crude oil fat)Gravity flow enters oil Fat baffle-box, grease temporary storage tank is delivered to by oil pump, periodically outward transport sale;Water enters liquid phase storage tank by pipeline self;Point The slag charge for separating out is by conveying worm conveying input liquid phase storage tank;Agitator is provided with liquid phase storage tank, three-phase separator is taken off Go out slag charge to be mutually sufficiently mixed with water, anaerobic fermentation system is delivered to by anaerobic system feed pump.
After adopting the above technical scheme, the utility model can rationally separate kitchen garbage, scientific utilization carries oil than tradition System oil extracting rate improves 3% or so, lifts the rate of recovery of kitchen garbage.The utility model includes wet solution tank, pressure surge tank, thick Thin squeezer and oil-water separation system, wet solution tank carry out wet solution treatment under given temperature and pressure, and kitchen garbage is made in wet solution The vegetable and animals oils being incorporated under in material are sufficiently separated out, while reducing material viscosity, make the inorganic matter that density is larger Easily settle, separate, and the organic matter in material is dissolved, fiber is refined, and reduces material viscosity coefficient, possesses good Mobility.Pressure surge tank has makes material be cached in pressure surge tank, the effect of pressure release and cooling, it is ensured that in follow-up work It is smoothed out in work.Thickness squeezer can by the impurity in material after wet solution carry out mechanical expression dehydration, heavy gravel sedimentation with And the abjection of long fibre organic matter, three-phase separator is re-fed into by feed separation into oil, water, the part of slag three, resource is made full use of, Decompose material to maximize, impurity-eliminating effect is improved, water-oil separating is more thorough, in hgher efficiency, rate of recovery lifting.
Preferred embodiment of the present utility model is the foregoing is only, is not used to limit the utility model, it is all at this Any modification, equivalent and improvement made within the spirit and principle of utility model etc., should be included in the utility model Protection domain within.

Claims (4)

1. a kind of oil-containing material high carries oil system, it is characterised in that:Including wet solution tank(1), pressure surge tank(2), thickness squeezing Machine(3)And oil-water separation system(4), the wet solution tank(1)With pressure surge tank(2)Between conveyance conduit on be connected with conveying Pump one(5), the pressure surge tank(2)With thickness squeezer(3)Between conveyance conduit on be connected with delivery pump two(6), institute State thickness squeezer(3)With oil-water separation system(4)Between conveyance conduit on be connected with delivery pump three(7);
The thickness squeezer includes:Thick squeezer(31), gravity riffler(32)With thin squeezer(33), the thick squeezer Material charging aperture(311)With the pressure surge tank discharging opening(22)It is connected, thick squeezer material squeezes discharging opening(312)With institute State gravity riffler charging aperture(321)It is connected, the gravity riffler discharging opening(322)With the thin squeezing machine inlet (331)It is connected, the thin squeezer discharging opening(332)With the oil-water separation system(4)In mixed liquor tank diameter(41)It is logical Piping is connected;
The oil-water separation system(4)Including mixed liquor tank diameter(41), three-phase separator(42)With attached tank body, the mixing Liquid tank diameter(41)With three-phase separator(42)Between be connected with and make the three-phase separator(42)Inlet amount stabilization rotor Pump, the impeller pump uses VFC.
2. oil-containing material high according to claim 1 carries oil system, it is characterised in that the wet solution tank(1)Using steam Directly heat, the wet solution tank(1)Including automatic control system, automatic control system is to the temperature in course of reaction, pressure, liquid Position and heat time are automatically controlled.
3. oil-containing material high according to claim 1 carries oil system, it is characterised in that the thick squeezer discharging opening(31) Including squeezing discharging opening(312)With impurity discharging opening, the thick squeezer will can separate in material more than the impurity of 12mm, And mechanical expression dehydration is carried out to impurity, the impurity after squeezing is delivered to debris by impurity discharging opening by enclosed belt conveyor Transhipment is stored between accumulating.
4. oil-containing material high according to claim 1 carries oil system, it is characterised in that the gravity riffler(32)Also wrap Sand setting mechanism is included, the sand setting mechanism is arranged in cell body, being acted on by gravitational settling settles the heavy gravel in material.
CN201621179322.8U 2016-10-27 2016-10-27 A kind of oil-containing material high carries oil system Active CN206240916U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201621179322.8U CN206240916U (en) 2016-10-27 2016-10-27 A kind of oil-containing material high carries oil system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201621179322.8U CN206240916U (en) 2016-10-27 2016-10-27 A kind of oil-containing material high carries oil system

Publications (1)

Publication Number Publication Date
CN206240916U true CN206240916U (en) 2017-06-13

Family

ID=58997215

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201621179322.8U Active CN206240916U (en) 2016-10-27 2016-10-27 A kind of oil-containing material high carries oil system

Country Status (1)

Country Link
CN (1) CN206240916U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107876550A (en) * 2017-12-12 2018-04-06 广东利世康低碳科技有限公司 A kind of kitchen garbage pretreatment system of energy high efficiente callback organic matter
CN108822968A (en) * 2018-05-28 2018-11-16 长沙中联重科环境产业有限公司 Boiling proposes oily smart feeding system and its control method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107876550A (en) * 2017-12-12 2018-04-06 广东利世康低碳科技有限公司 A kind of kitchen garbage pretreatment system of energy high efficiente callback organic matter
CN108822968A (en) * 2018-05-28 2018-11-16 长沙中联重科环境产业有限公司 Boiling proposes oily smart feeding system and its control method
CN108822968B (en) * 2018-05-28 2021-12-24 长沙中联重科环境产业有限公司 Intelligent feeding system for cooking oil extraction and control method thereof

Similar Documents

Publication Publication Date Title
CN105925361B (en) The preprocess method of anaerobic digestion of kitchen wastes processing
CN101224999B (en) Anaerobic digestion handling method for restaurant garbage
CN102688881B (en) Urban kitchen waste recycling and innoxious process for treating
CN102601101B (en) A kind of method that realizes changing food waste harmless treatment and comprehensive utilization
CN101927254B (en) Comprehensive food waste treatment system and treatment method thereof
CN206122316U (en) Kitchen garbage handles all -in -one
CN110343726A (en) A kind of cooperative processing method of food garbage and rubbish from cooking
CN205008375U (en) Waste disposal equipment
CN105414158B (en) A kind of anaerobic fermentation for kitchen garbage couples the processing method of hydrothermal liquefaction
CN103074381A (en) Efficient resourceful treatment method through separation and anaerobic fermentation for kitchen waste
CN109365480A (en) Rubbish from cooking and kitchen garbage collaboration processing equipment and processing method
CN202860973U (en) Kitchen garbage treatment equipment
CN103121859A (en) Kitchen waste on-site treatment method
CN102489496A (en) Method for carrying out anaerobic digestion on kitchen waste after heat-moisture treatment
CN102873078A (en) Kitchen garbage disposal method
CN103272830A (en) Harmless treatment process of kitchen wastes
CN104907316B (en) A kind of kitchen garbage and civic feces total system and its method
CN102492556A (en) Treatment method for extracting grease from kitchen waste and performing biogas fermentation on kitchen waste
CN206810847U (en) Kitchen garbage energy, Fertilizer Transformed and fodder fusion processing system
CN101574701A (en) Treatment method and system of restaurant waste
CN111318552A (en) Kitchen waste pretreatment device and pretreatment method
CN112517615A (en) Organic matter combined anaerobic pretreatment device and method
CN206240916U (en) A kind of oil-containing material high carries oil system
CN104232690B (en) The processing method of kitchen garbage
CN102502956A (en) Municipal organic waste combined anaerobic treatment process and equipment

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant