CN105219514B - The treatment process and refine system automatically that a kind of Non-intermittent formula commercial grease refines - Google Patents
The treatment process and refine system automatically that a kind of Non-intermittent formula commercial grease refines Download PDFInfo
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- CN105219514B CN105219514B CN201510619206.7A CN201510619206A CN105219514B CN 105219514 B CN105219514 B CN 105219514B CN 201510619206 A CN201510619206 A CN 201510619206A CN 105219514 B CN105219514 B CN 105219514B
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Abstract
The present invention relates to the treatment process that a kind of Non-intermittent formula commercial grease refines, it includes the processes such as metering, broken, refinement, dregs of fat separation, squeezing, gas sampling and exhaust-gas treatment, the invention further relates to the automatic refinement systems that a kind of Non-intermittent formula commercial grease refines, it is characterized in that, it includes self-measuring device, rough and torn crushing device, smart crushing device, device for refining, oil residue separating apparatus, lard press, waste gas collection device, emission-control equipment and dregs of fat measuring packing machine, oil liquid storage tank and automatic control system；A kind of refine the object of the present invention is to provide Non-intermittent formula commercial grease treatment process and refine system automatically, using treatment process of the invention and refine system, the oil refining of Non-intermittent may be implemented, the temperature of extractive process different phase is preferably controlled simultaneously, improve the quality of oil refining, the dregs of fat and exhaust gas are all handled simultaneously, the utilization of the dregs of fat is also improved while environmentally friendly.
Description
Technical field
The present invention relates to the processing that animal fats industry refines field more particularly to a kind of refinement of Non-intermittent formula commercial grease
Technique and system is refined automatically.
Background technique
With the development of industrial society, the demand to animal fat be also increasing, traditional industrial extraction method with
Based on squeezing, squeeze using Smashing extraction method, to be easy to cause in grease containing more impurity, with science and technology into
The development of step and society, present industrial abstract mode is all refined by the way of hot oil refining mostly, existing to mention
Refining all is very coarse mostly, and temperature control inaccuracy in oil refining process, the temperature of conduction oil is substantially a definite value, can be led in this way
Phenomena such as causing the animal oil refining out to burn, influences the quality of oil refining, while also not to the processing of exhaust gas and the dregs of fat
In place, cause entire utilization rate not high, while existing oil refining apparatus requires manual operation mostly, centre needs to pause, no
It is able to achieve the production of Non-intermittent formula.
By patent retrieval, there are following known prior arts:
Patent 1:
Application number: 201210241360.1, the applying date: 2012-07-13, authorized announcement date: 2014-01-29, this project
Related production technology, in process, using medium temperature soft water wash, and add phosphoric acid or citric acid chelating heavy metal from
Son, a possibility that reducing Oxidation of Fat and Oils；For the quality for guaranteeing edible oil；Guarantee the ring in vacuum in dehydration, bleaching process
It is carried out under border；The stability that depickling, deodorization procedures add a certain amount of citric acid to make grease is guaranteed, and physical deacidification, deodorization exist
Oil yield is high, high-quality under high vacuum；It is adjusted using automatic temperature-adjusting, ensures product quality；Vacuum line is set, guarantees vacuum
Environment；Using continuously or semi-continuously production method, shorten oil product cycle period.
Patent 2:
Application number: 201320511002.8, the applying date: 2013-08-20, data of publication of application: 2014-02-05, the present invention
Disclose a kind of animal fat processing equipment field more particularly to a kind of oil residue separating apparatus, the fuel reserve tank including a upper opening,
One rotary screen is laterally set at the fuel reserve tank upper opening；The aperture of rotary screen end passes through the refining above pipeline and end
Oily device connection, is equipped with a driving wheel in the fuel reserve tank sidewall below rotary screen one end, and the driving wheel and drum screen are logical
Cross gear mesh；On the fuel reserve tank, it is equipped with a motor with the ipsilateral side wall of driving wheel, the motor is by conveyer belt and passes
Driving wheel is connected.This kind of oil residue separating apparatus, it is easy to operate, it is easy to use, manpower can be saved, working efficiency and safety are improved
Property, the separation of oil and slag suitable for animal fat treatment process.
Patent 3:
Application number: 201420600173.2, the applying date: 2014-10-16, data of publication of application: 2015-02-11, the present invention
A kind of extraction system for proposing rouge equipment and full-automation of animal oil is disclosed, it includes with feed inlet, fuel-displaced that this, which proposes rouge equipment,
Mouthful, slag notch mention rouge pot；Positioned at mentioning rouge pot inner heating device；It is arranged in and mentions stirring along the setting of its own short transverse in rouge pot
Mix axis；The blade being fixed on agitating shaft；And the driving motor for driving agitating shaft to rotate, it is set in particular, mentioning rouge
Standby further includes that the dregs of fat that mention in rouge pot can by screen that oil is separated with the dregs of fat and after being used to separate are arranged in from slag notch row
Residue extraction pipeline and residual cake valve out, wherein screen periphery and the inner wall comprehensive engagement for proposing rouge pot circumferential direction, and screen is located at blade
Lower section.The utility model good mixing effect, reliability and stability are good and easy to maintenance.The utility model animal oil extraction system
Oil yield is high, basic non-environmental-pollution, labor intensity of workers are small, meanwhile, structure is simple, easy to implement, very useful.
Through the above search, it has been found that above technical scheme cannot influence novelty of the invention；And the above patent text
The intercombination of part cannot destroy creativeness of the invention.
Summary of the invention
A kind of refine the object of the present invention is to provide Non-intermittent formula commercial grease treatment process and automatically system is refined, adopted
With treatment process of the invention and system is refined, the oil refining of Non-intermittent may be implemented, while preferably controlling extractive process not
With the temperature in stage, the quality of oil refining is improved, while the dregs of fat and exhaust gas are all handled, is also improved while environmentally friendly
The utilization of the dregs of fat.
In order to achieve the goal above, the technical solution adopted by the present invention are as follows: a kind of place that Non-intermittent formula commercial grease refines
Science and engineering skill, it includes the following steps:
1., metering, the frost raw material of animal tallow or fresh material are subjected to Weighing by self-measuring device；
2., it is broken, 1. raw material that step measures is transported in crusher by automatic transportation band and is crushed, after being crushed
Raw material be diameter 8-12mm particle；
3., refine, step 2. broken particulate material by material conveying flood dragon send to the extraction slot of device for refining,
In extraction slot, preceding 30min is heating, and the temperature of conduction oil is 220-260 DEG C, promotes temperature of charge to 150 DEG C, 30-
60min be it is fuel-displaced, the temperature of conduction oil is 230-250 DEG C, and temperature of charge is 200 DEG C and starts a large amount of fuel-displaced, and 60-90min is to endure
System, at 150-170 DEG C, 90-120min is discharging for temperature of charge control, and temperature of charge is 115-125 DEG C, and material is transported to next
In grade extraction slot, above-mentioned extractive process is repeated by 3-6 section extraction slot；
4., the dregs of fat separation, the 3. dregs of fat that step is extract from the dregs of fat outlet enters oil residue separating apparatus carry out the dregs of fat
Separation, the oil liquid a part separated are sent by repairing pipe to progress repairing heating in first segment extraction slot, another part warp
It send after flowmeter metering to oil liquid hold-up tank；
5., squeezing, the 4. dregs of fat that step is separated send to lard press through vertical flood dragon and are squeezed, and squeezing obtains
Oil liquid sent after flowmeter measures to oil liquid hold-up tank, slag carries out filling packet storage through dregs of fat measuring packing machine；
6., gas sampling, 3. step is refined and 4. exhaust gas that step generates in dregs of fat separating step is by gas sampling
Device is collected；
7. exhaust-gas treatment, by step, 6. the middle exhaust gas collected is passed through emission-control equipment progress exhaust-gas treatment.
Preferably, step 2. in crusher include rough and torn crushing device and smart crushing device, break off the particulate material come
Diameter is 10mm.
Preferably, step is 3. in extractive process, and in extraction slot, the temperature of conduction oil is 240 DEG C in preceding 30min, 30-
The temperature of 60min conduction oil is 240 DEG C, and 60-90min temperature of charge is 160 DEG C, and 90-120min temperature of charge is 120 DEG C.
Preferably, step have passed through 5 section extraction slots and repeat to refine 3. in extractive process.
The automatic refinement system that a kind of Non-intermittent formula commercial grease of another scheme of the invention refines, it includes automatic meter
Device is measured, for the self-measuring device by automatic transportation band connection to rough and torn crushing device, it is broken that rough and torn crushing device is connected to essence
Crushing device, the smart crushing device convey flood dragon by material and are connected to device for refining, and the device for refining is connected with oil
The flowline (5) of slag separator, the oil residue separating apparatus is connected to oil liquid by flow gauge and repairing pipe respectively
The residue outlet (6) of hold-up tank and device for refining, oil residue separating apparatus is connected to lard press, the dregs of fat through vertical flood dragon
The oil outlet of squeezer is by flow gauge is connected to oil liquid hold-up tank, slag notch is connected to dregs of fat measuring packing machine；It is described
Device for refining, oil residue separating apparatus and lard press be respectively connected with waste gas collection device, waste gas collection device is connected to useless
Flash Gas Compression Skid System；The self-measuring device, rough and torn crushing device, smart crushing device, device for refining, oil residue separating apparatus, oil
Slag squeezer, waste gas collection device, emission-control equipment and dregs of fat measuring packing machine are all connected to automatic control system.
Further, the device for refining saves inclined extraction slot (13) by 3-6 and is formed by connecting from beginning to end, and a upper section mentions
The feed inlet docking of the discharge port and next section extraction slot (13) of slot (13) is refined, the feed inlet of first segment extraction slot (13) is combined with
Feed pipe (11), the discharge port of final section extraction slot (13) are that the dregs of fat export (1), the inside setting of the extraction slot (13)
Have push flood dragon (12), the outer cover heat-conducting layer (14) thermally conductive using conduction oil；The extraction slot (13) and heat-conducting layer (14)
Inside is provided with temperature inductor, and temperature inductor is connect with the electric temperature control valve in controller.
Further, the extraction slot (13) is cylindrical shape, and the inclined height of its end is not more than extraction slot (13)
Radius.
Further, the oil residue separating apparatus includes the dregs of fat separation that the dregs of fat export the setting that is tilted to the right below (1)
Band (3), the dregs of fat separation band (3) are driven by its internal roller (2)；It is set below the dregs of fat separation band (3)
It is equipped with and the consistent separating tank of its gradient (4), the bottom left end of the separating tank (4) is provided with flowline (5), bottom, right
End is provided with residue outlet (6)；It is characterized in that, being provided with rotating cylinder (9) in the separating tank (4), and the right end of rotating cylinder (9) connects
It is connected on the motor (8) being arranged on the outside of separating tank (4), is provided on the rotating cylinder (9) helical blade (10), and helical blade
(10) it is located at immediately below dregs of fat outlet (1) between residue outlet (6).
Further, it is provided with partition (7) on the bottom interior surface of the separating tank (4), and the upper end of partition (7) is left
Side is located on the underface extended line of dregs of fat outlet (1) rightmost side, and the rotating cylinder (9) is located at partition (7) and separating tank (4)
Between right side wall.
Further, the lower portion oil filtering plate for oil (701) of the partition (7)；The outer edge of the bolt blade (10)
Position is oil strain layer (1001).
The invention has the benefit that
1, technique of the invention uses full-automatic equipment, and the oil refining of Non-intermittent, while preferable control may be implemented
The temperature for having made extractive process different phase improves the quality of oil refining, prevents situations such as fat is burnt appearance.
2, the dregs of fat and exhaust gas are all handled in technique of the invention, the dregs of fat is squeezed, it can will wherein
The oil liquid not refined squeeze out come, while also can the remaining dregs of fat carried out fill packet utilize, substantially increase economic benefit；Tail gas
Collection and vent gas treatment can be recycled water vapour therein, without sewage discharge, while also protect environment.
3, more piece extraction slot is used in extractive process to repeat to refine, the oil yield of refinement can be improved, and improves economic effect
Fruit.
4, the device of the invention have passed through controller whole-process control, realize automated job, while nothing also may be implemented
Batch operation substantially increases the efficiency of operation, reduces manpower work.
5, it is provided with temperature sensor in extraction slot and in oil refining layer, and is connected to the temperature control valve in controller,
It can be very good to control the temperature in each period in extraction slot and oil refining layer, guarantee the stability of oil refining, substantially increase
The quality of oil refining.
6, a propulsion spiral flood dragon is set in the separating tank of oil residue separating apparatus, separation can be fallen with middle part
The dregs of fat are pushed to end by spiral flood dragon, and come out from the slag notch of end, reduce the dregs of fat mixed volume in oil liquid, simultaneously
It there will not be the dregs of fat to deposit in separating tank, therefore do not need to clear up, the continuous dregs of fat separation of Non-intermittent may be implemented, be suitable for continuously
It has a rest grease frying production technology.
7, the design of partition can further prevent the dregs of fat to enter flowline, ensure that the oil liquid purity separated.
8, the oil filtering plate for oil design of the lower partition, it can only be by oil liquid molecule, and cannot be by the dregs of fat, and then can make oil
The oil liquid that slag separation band is not separated enters in flowline.
9, the oil strain layer of helical blade peripheral edge portion can only by oil liquid molecule, and cannot by the dregs of fat, and then can will
The oil liquid molecule for the omission that helical blade promotes can also make it into flowline, substantially increase the effect of separation.
Detailed description of the invention
Fig. 1 is a kind of structural schematic diagram for the automatic refinement system that Non-intermittent formula commercial grease refines.
Fig. 2 is the structural schematic diagram of device for refining.
Fig. 3 is the structural schematic diagram of oil residue separating apparatus.
Fig. 4 is the partial enlarged view of A in Fig. 3.
Fig. 5 is the partial enlarged view of B in Fig. 3.
Label character as shown in the figure indicates are as follows: 1, dregs of fat outlet；2, roller；3, the dregs of fat separate band；4, separating tank；5, fuel-displaced
Pipe；6, residue outlet；7, partition；8, motor；9, rotating cylinder；10, helical blade；11, feed pipe；12, flood dragon is pushed；13, extraction slot；
14, heat-conducting layer；701, oil filtering plate for oil；1001, oil strain layer.
Specific embodiment
In order to make those skilled in the art more fully understand technical solution of the present invention, with reference to the accompanying drawing to the present invention into
Row detailed description, the description of this part be only it is exemplary and explanatory, should not have any limitation to protection scope of the present invention
Effect.
As Figure 1-Figure 5, the automatic refinement system that a kind of Non-intermittent formula commercial grease of the present invention refines, it includes automatic
Metering device, the self-measuring device are connected to essence by automatic transportation band connection to rough and torn crushing device, rough and torn crushing device
Crushing device, the smart crushing device convey flood dragon by material and are connected to device for refining, and the device for refining is connected with
The flowline 5 of oil residue separating apparatus, the oil residue separating apparatus is connected to oil liquid by flow gauge and repairing pipe respectively
The residue outlet 6 of hold-up tank and device for refining, oil residue separating apparatus is connected to lard press, the dregs of fat pressure through vertical flood dragon
The oil outlet of crusher is by flow gauge is connected to oil liquid hold-up tank, slag notch is connected to dregs of fat measuring packing machine；Described
Device for refining, oil residue separating apparatus and lard press are respectively connected with waste gas collection device, and waste gas collection device is connected to exhaust gas
Processing unit；The self-measuring device, rough and torn crushing device, smart crushing device, device for refining, oil residue separating apparatus, the dregs of fat
Squeezer, waste gas collection device, emission-control equipment and dregs of fat measuring packing machine are all connected to automatic control system.
Preferably, the device for refining saves inclined 13 head and the tail of extraction slot by 3-6 and is formed by connecting, and upper section extraction slot
The docking of the feed inlet of 13 discharge port and next section extraction slot 13, the feed inlet of first segment extraction slot 13 are combined with feed pipe 11,
The discharge port of final section extraction slot 13 is dregs of fat outlet 1, and the extraction slot 13 is internally provided with push flood dragon 12, outside
The set heat-conducting layer 14 thermally conductive using conduction oil；It is provided with temperature inductor inside the extraction slot 13 and heat-conducting layer 14, and
Temperature inductor is connect with the electric temperature control valve in controller.
Preferably, the extraction slot 13 is cylindrical shape, and the inclined height of its end is not more than the radius of extraction slot 13.
Preferably, the oil residue separating apparatus includes the dregs of fat separation band 3 that the dregs of fat export the setting that is tilted to the right below 1,
The dregs of fat separation band 3 is driven by its internal roller 2；The lower section of the dregs of fat separation band 3 is provided with to be tilted with it
Consistent separating tank 4 is spent, the bottom left end of the separating tank 4 is provided with flowline 5, bottom right end is provided with residue outlet 6；Its
It is characterized in that, rotating cylinder 9 is provided in the separating tank 4, and the right end of rotating cylinder 9 is connected to the motor 8 being arranged on the outside of separating tank 4
On, be provided with helical blade 10 on the rotating cylinder 9, and helical blade 10 be located at immediately below dregs of fat outlet 1 and residue outlet 6 it
Between.
Preferably, it is provided with partition 7 on the bottom interior surface of the separating tank 4, and is located at oil on the left of the upper end of partition 7
Slag exports on the underface extended line of 1 rightmost side, and the rotating cylinder 9 is between partition 7 and the right side wall of separating tank 4.
Preferably, the lower portion oil filtering plate for oil 701 of the partition 7；The outer rim position of the bolt blade 10 is oil strain
Layer 1001.
Wherein the work of oil residue separating apparatus is as follows: oil and slag come out from dregs of fat outlet 1 together, drop into the dregs of fat point later
From on band 3, oil liquid is directly dropped into separating tank 4 from the mesh on dregs of fat separation band 3, and then goes out from flowline 5, the dregs of fat
Band 3 can be separated with the dregs of fat by the oil liquid that the dregs of fat block with a part of part to travel forward, the small dregs of fat in part and oil liquid can be with oil
The movement of slag separation band 3 is gradually fallen, and the remaining dregs of fat can be fallen from the right end that the dregs of fat separate band 3, enters finally into residue outlet 6
In, and the oil liquid that middle part is fallen can enter by the oil filtering plate for oil 701 of 7 lower part of edge oil strain layer 1001 and partition of helical blade 10
Into flowline 5, and the dregs of fat that middle part is fallen can enter eventually into residue outlet 6 under the drive of helical blade 10.
Embodiment using a kind for the treatment of process of Non-intermittent formula commercial grease refinement of above equipment is as follows:
Embodiment 1
1., metering, the frost raw material of animal tallow or fresh material are subjected to Weighing by self-measuring device；
2., it is broken, 1. raw material that step measures transports rough and torn crushing device and smart crushing device by automatic transportation band
In be crushed, broken raw material be diameter 10mm particle；
3., refine, step 2. broken particulate material by material conveying flood dragon send to the extraction slot of device for refining,
In extraction slot, preceding 30min is heating, and the temperature of conduction oil is 240 DEG C, promotes temperature of charge to 150 DEG C, and 30-60min is
Fuel-displaced, the temperature of conduction oil is 240 DEG C, and temperature of charge is that 200 DEG C of beginnings are a large amount of fuel-displaced, and 60-90min is tanning, temperature of charge
At 160 DEG C, 90-120min is discharging for control, and temperature of charge is 120 DEG C, and material is transported in next stage extraction slot, by 5 sections
Extraction slot repeats above-mentioned extractive process；
4., the dregs of fat separation, the 3. dregs of fat that step is extract from the dregs of fat outlet enters oil residue separating apparatus carry out the dregs of fat
Separation, the oil liquid a part separated are sent by repairing pipe to progress repairing heating in first segment extraction slot, another part warp
It send after flowmeter metering to oil liquid hold-up tank；
5., squeezing, the 4. dregs of fat that step is separated send to lard press through vertical flood dragon and are squeezed, and squeezing obtains
Oil liquid sent after flowmeter measures to oil liquid hold-up tank, slag carries out filling packet storage through dregs of fat measuring packing machine；
6., gas sampling, 3. step is refined and 4. exhaust gas that step generates in dregs of fat separating step is by gas sampling
Device is collected；
7. exhaust-gas treatment, by step, 6. the middle exhaust gas collected is passed through emission-control equipment progress exhaust-gas treatment.
Embodiment 2
1., metering, the frost raw material of animal tallow or fresh material are subjected to Weighing by self-measuring device；
2., it is broken, 1. raw material that step measures transports rough and torn crushing device and smart crushing device by automatic transportation band
In be crushed, broken raw material be diameter 8mm particle；
3., refine, step 2. broken particulate material by material conveying flood dragon send to the extraction slot of device for refining,
In extraction slot, preceding 30min is heating, and the temperature of conduction oil is 260 DEG C, promotes temperature of charge to 150 DEG C, and 30-60min is
Fuel-displaced, the temperature of conduction oil is 230 DEG C, and temperature of charge is that 200 DEG C of beginnings are a large amount of fuel-displaced, and 60-90min is tanning, temperature of charge
At 170 DEG C, 90-120min is discharging for control, and temperature of charge is 115 DEG C, and material is transported in next stage extraction slot, by 3 sections
Extraction slot repeats above-mentioned extractive process；
4., the dregs of fat separation, the 3. dregs of fat that step is extract from the dregs of fat outlet enters oil residue separating apparatus carry out the dregs of fat
Separation, the oil liquid a part separated are sent by repairing pipe to progress repairing heating in first segment extraction slot, another part warp
It send after flowmeter metering to oil liquid hold-up tank；
5., squeezing, the 4. dregs of fat that step is separated send to lard press through vertical flood dragon and are squeezed, and squeezing obtains
Oil liquid sent after flowmeter measures to oil liquid hold-up tank, slag carries out filling packet storage through dregs of fat measuring packing machine；
6., gas sampling, 3. step is refined and 4. exhaust gas that step generates in dregs of fat separating step is by gas sampling
Device is collected；
7. exhaust-gas treatment, by step, 6. the middle exhaust gas collected is passed through emission-control equipment progress exhaust-gas treatment.
Embodiment 3
1., metering, the frost raw material of animal tallow or fresh material are subjected to Weighing by self-measuring device；
2., it is broken, 1. raw material that step measures transports rough and torn crushing device and smart crushing device by automatic transportation band
In be crushed, broken raw material be diameter 12mm particle；
3., refine, step 2. broken particulate material by material conveying flood dragon send to the extraction slot of device for refining,
In extraction slot, preceding 30min is heating, and the temperature of conduction oil is 220 DEG C, promotes temperature of charge to 150 DEG C, and 30-60min is
Fuel-displaced, the temperature of conduction oil is 250 DEG C, and temperature of charge is that 200 DEG C of beginnings are a large amount of fuel-displaced, and 60-90min is tanning, temperature of charge
At 150 DEG C, 90-120min is discharging for control, and temperature of charge is 125 DEG C, and material is transported in next stage extraction slot, by 6 sections
Extraction slot repeats above-mentioned extractive process；
4., the dregs of fat separation, the 3. dregs of fat that step is extract from the dregs of fat outlet enters oil residue separating apparatus carry out the dregs of fat
Separation, the oil liquid a part separated are sent by repairing pipe to progress repairing heating in first segment extraction slot, another part warp
It send after flowmeter metering to oil liquid hold-up tank；
5., squeezing, the 4. dregs of fat that step is separated send to lard press through vertical flood dragon and are squeezed, and squeezing obtains
Oil liquid sent after flowmeter measures to oil liquid hold-up tank, slag carries out filling packet storage through dregs of fat measuring packing machine；
6., gas sampling, 3. step is refined and 4. exhaust gas that step generates in dregs of fat separating step is by gas sampling
Device is collected；
7. exhaust-gas treatment, by step, 6. the middle exhaust gas collected is passed through emission-control equipment progress exhaust-gas treatment.
It should be noted that, in this document, the terms "include", "comprise" or its any other variant are intended to non-row
His property includes, so which element is the process, method, article or equipment for including a series of elements not only include, and
And further include other elements that are not explicitly listed, or further include for this process, method, article or equipment institute it is intrinsic
Element.
Used herein a specific example illustrates the principle and implementation of the invention, the explanation of above example
It is merely used to help understand method and its core concept of the invention.The above is only a preferred embodiment of the present invention, it answers
When pointing out due to the finiteness of literal expression, and objectively there is unlimited specific structure, for the common skill of the art
For art personnel, without departing from the principle of the present invention, several improvement, retouching or variation can also be made, can also incited somebody to action
Above-mentioned technical characteristic is combined in the right way；These improve retouching, variation or combination, or the not improved structure by invention
Think and technical solution directly applies to other occasions, is regarded as protection scope of the present invention.
Claims (4)
1. the treatment process that a kind of Non-intermittent formula commercial grease refines, which is characterized in that its treatment process includes the following steps:
1., metering, the frost raw material of animal tallow or fresh material are subjected to Weighing by self-measuring device；
2., it is broken, 1. raw material that step measures is transported in crusher by automatic transportation band and is crushed, broken original
Material is the particle of diameter 8-12mm；
3., refine, step 2. broken particulate material by material conveying flood dragon send to the extraction slot of device for refining, mentioning
It refines in slot, preceding 30min is heating, and the temperature of conduction oil is 220-260 DEG C, promotes temperature of charge to 150 DEG C, and 30-60min is
Fuel-displaced, the temperature of conduction oil is 230-250 DEG C, and temperature of charge is that 200 DEG C of beginnings are a large amount of fuel-displaced, and 60-90min is tanning, material
At 150-170 DEG C, 90-120min is discharging for temperature control, and temperature of charge is 115-125 DEG C, and material is transported to next stage refinement
In slot, above-mentioned extractive process is repeated by 3-6 section extraction slot；
4., the dregs of fat separation, the 3. dregs of fat that step is extract from the dregs of fat outlet enters oil residue separating apparatus carry out dregs of fat separation,
The oil liquid a part separated is sent by repairing pipe to progress repairing heating in first segment extraction slot, and another part is through flowmeter
It is sent after metering to oil liquid hold-up tank；
5., squeezing, the 4. dregs of fat that step is separated send to lard press the oil for being squeezed, being squeezed through vertical flood dragon
Liquid is sent after flowmeter measures to oil liquid hold-up tank, and slag carries out filling packet storage through dregs of fat measuring packing machine；
6., gas sampling, 3. step is refined and 4. exhaust gas that step generates in dregs of fat separating step is by waste gas collection device
It is collected；
7. exhaust-gas treatment, by step, 6. the middle exhaust gas collected is passed through emission-control equipment progress exhaust-gas treatment；
A kind of Non-intermittent formula commercial grease refines and refines system automatically applied by treatment process, it includes self-measuring device,
The self-measuring device is connected to smart crushing device, institute by automatic transportation band connection to rough and torn crushing device, rough and torn crushing device
The smart crushing device stated conveys flood dragon by material and is connected to device for refining, and the device for refining is connected with dregs of fat separation dress
It sets, the flowline (5) of the oil residue separating apparatus is connected to oil liquid hold-up tank and refinement by flowmeter and repairing pipe respectively
Device, the residue outlet (6) of oil residue separating apparatus are connected to lard press through vertical flood dragon, the lard press it is fuel-displaced
Mouth is by flowmeter is connected to oil liquid hold-up tank, slag notch is connected to dregs of fat measuring packing machine；The device for refining, the dregs of fat point
It is respectively connected with waste gas collection device from device and lard press, waste gas collection device is connected to emission-control equipment；Described
Self-measuring device, rough and torn crushing device, smart crushing device, device for refining, oil residue separating apparatus, lard press, gas sampling
Device, emission-control equipment and dregs of fat measuring packing machine are all connected to automatic control system；The device for refining is inclined by 3-6 section
Oblique extraction slot (13) is formed by connecting from beginning to end, and the charging of the discharge port and next section extraction slot (13) of upper section extraction slot (13)
Mouth docking, the feed inlet of first segment extraction slot (13) are combined with feed pipe (11), and the discharge port of final section extraction slot (13) is
The dregs of fat export (1), and the extraction slot (13) is internally provided with push flood dragon (12), and outer cover is led using conduction oil is thermally conductive
Thermosphere (14)；Temperature inductor, and temperature inductor and control are provided with inside the extraction slot (13) and heat-conducting layer (14)
Electric temperature control valve connection in device processed；The oil residue separating apparatus includes the oil that the dregs of fat export the setting that is tilted to the right below (1)
Slag separation band (3), the dregs of fat separation band (3) are driven by its internal roller (2)；The dregs of fat separation band (3)
Lower section be provided with the consistent separating tank of its gradient (4), the bottom left end of the separating tank (4) be provided with flowline (5),
Bottom right end is provided with residue outlet (6)；It is provided with rotating cylinder (9) in the separating tank (4), and the right end of rotating cylinder (9) is connected to
On the motor (8) being arranged on the outside of separating tank (4), it is provided on the rotating cylinder (9) helical blade (10), and helical blade (10)
Immediately below dregs of fat outlet (1) between residue outlet (6)；Partition is provided on the bottom interior surface of the separating tank (4)
(7), and on the left of the upper end of partition (7) it is located on the underface extended line of dregs of fat outlet (1) rightmost side, the rotating cylinder (9) position
Between partition (7) and the right side wall of separating tank (4)；The lower portion of the partition (7) is oil filtering plate for oil (701)；The spiral shell
The outer rim position of vane piece (10) is oil strain layer (1001).
2. the treatment process that a kind of Non-intermittent formula commercial grease according to claim 1 refines, which is characterized in that step is 2.
In crusher include rough and torn crushing device and smart crushing device, breaking off the particulate material diameter come is 10mm.
3. the treatment process that a kind of Non-intermittent formula commercial grease according to claim 1 refines, which is characterized in that step is 3.
In extractive process, in extraction slot (13), the temperature of conduction oil is 240 DEG C in preceding 30min, and the temperature of 30-60min conduction oil is
240 DEG C, 60-90min temperature of charge is 160 DEG C, and 90-120min temperature of charge is 120 DEG C.
4. the treatment process that a kind of Non-intermittent formula commercial grease according to claim 1 refines, which is characterized in that described
Extraction slot (13) is cylindrical shape, and the inclined height of its end is not more than the radius of extraction slot (13).
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| CN113828193B (en) * | 2021-09-23 | 2024-04-05 | 江苏德康医疗器械有限公司 | Mink oil extraction element for cosmetics |
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Effective date of registration: 20220302 Address after: Upper formation of Zhongcun village, Baixiang Town, Yueyang County, Yueyang City, Hunan Province Patentee after: Hunan Xiangbai Eco-environmental Protection Technology Co.,Ltd. Address before: 4100 No. 10, Shangbian group, xiequn village, Baixiang Town, Yueyang County, Yueyang City, Hunan Province Patentee before: Xie Songbai |