CN105219514A - The treatment process that a kind of Non-intermittent formula commercial grease refines and automatically refine system - Google Patents
The treatment process that a kind of Non-intermittent formula commercial grease refines and automatically refine system Download PDFInfo
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- CN105219514A CN105219514A CN201510619206.7A CN201510619206A CN105219514A CN 105219514 A CN105219514 A CN 105219514A CN 201510619206 A CN201510619206 A CN 201510619206A CN 105219514 A CN105219514 A CN 105219514A
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- 238000000034 method Methods 0.000 title claims abstract description 43
- 239000004519 grease Substances 0.000 title claims abstract description 28
- 238000007670 refining Methods 0.000 claims abstract description 42
- 239000012530 fluid Substances 0.000 claims abstract description 38
- 239000002912 waste gas Substances 0.000 claims abstract description 29
- 239000007789 gas Substances 0.000 claims abstract description 18
- 238000013467 fragmentation Methods 0.000 claims abstract description 16
- 238000006062 fragmentation reaction Methods 0.000 claims abstract description 16
- 238000004806 packaging method and process Methods 0.000 claims abstract description 12
- 238000000926 separation method Methods 0.000 claims abstract description 7
- 238000005070 sampling Methods 0.000 claims abstract description 6
- 239000003921 oil Substances 0.000 claims description 100
- 238000000605 extraction Methods 0.000 claims description 65
- 239000002994 raw material Substances 0.000 claims description 15
- 239000002893 slag Substances 0.000 claims description 13
- 238000010438 heat treatment Methods 0.000 claims description 11
- 239000011236 particulate material Substances 0.000 claims description 7
- 238000007599 discharging Methods 0.000 claims description 6
- 238000011049 filling Methods 0.000 claims description 6
- 238000001914 filtration Methods 0.000 claims description 6
- 238000009835 boiling Methods 0.000 claims description 5
- 238000007710 freezing Methods 0.000 claims description 5
- 230000008014 freezing Effects 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 5
- 239000002245 particle Substances 0.000 claims description 5
- 239000003760 tallow Substances 0.000 claims description 5
- 238000005303 weighing Methods 0.000 claims description 5
- 238000003032 molecular docking Methods 0.000 claims description 3
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 239000003925 fat Substances 0.000 description 87
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 6
- 239000000446 fuel Substances 0.000 description 4
- 239000010775 animal oil Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 238000004332 deodorization Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004061 bleaching Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 239000008157 edible vegetable oil Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000008234 soft water Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Edible Oils And Fats (AREA)
- Fats And Perfumes (AREA)
Abstract
The present invention relates to the treatment process that a kind of Non-intermittent formula commercial grease refines, it comprises the operations such as metering, fragmentation, refinement, dregs of fat separation, squeezing, gas sampling and off gas treatment, the invention still further relates to the automatic refinement system that a kind of Non-intermittent formula commercial grease refines, it is characterized in that, it comprises self-measuring device, coarse breaking device, smart shredder assembly, device for refining, oil residue separating apparatus, lard press, waste gas collection device, emission-control equipment and dregs of fat metering packaging machine, fluid storage tank and automatic control system; The object of this invention is to provide the treatment process of a kind of Non-intermittent formula commercial grease refinement and automatically refine system, adopt treatment process of the present invention and refinement system, the oil refining of Non-intermittent can be realized, control the temperature of extractive process different steps preferably simultaneously, improve the quality of oil refining, the dregs of fat and waste gas are all processed simultaneously, while environmental protection, also improve the utilization of the dregs of fat.
Description
Technical field
The present invention relates to animal fats industry and refine field, particularly relate to the treatment process of a kind of Non-intermittent formula commercial grease refinement and automatically refine system.
Background technology
Along with the development of industrial society, also be increasing to the demand of animal grease, traditional industrial extraction method is based on squeezing, what squeezing adopted is Smashing extraction method, thus easily cause in grease containing more impurity, along with the progress of science and technology and the development of society, the mode that present industrial abstract mode all have employed deep fat refining is mostly refined, existing refinement is all very coarse mostly, in oil refining process, temperature controls inaccurate, the temperature of thermal oil is a definite value substantially, the animal oil refining out can be caused like this to occur phenomenons such as burning, have influence on the quality of oil refining, simultaneously also not in place to the process of waste gas and the dregs of fat, cause whole utilization ratio not high, existing oil refining apparatus all needs manual operation mostly simultaneously, intermediate demand pauses, Non-intermittent formula can not be realized produce.
By patent retrieval, there is following known prior art:
Patent 1:
Application number: 201210241360.1, the applying date: 2012-07-13, authorized announcement date: 2014-01-29, production technology involved by this project, in process, warm soft water washing in employing, and add phosphoric acid or citric acid sequester heavy metal ions, decrease the possibility of Oxidation of Fat and Oils; For ensureing the quality of edible oil; Carry out ensure the environment in vacuum in dehydration, bleaching process under; Depickling, deodorization procedures add a certain amount of citric acid makes the stability of grease be guaranteed, and oil yield is high under a high vacuum, quality good for physical deacidification, deodorization; Employing automatic temp regulates, products quality guarantee; Vacuum-lines is set, ensures vacuum environment; Adopt continuous or semi-successive cultivation mode, shorten oil product loop cycle.
Patent 2:
Application number: 201320511002.8, the applying date: 2013-08-20, Shen Qing Publication day: 2014-02-05, the invention discloses a kind of animal grease treatment facility field, particularly relate to a kind of oil residue separating apparatus, comprise the fuel reserve tank of a upper shed, described fuel reserve tank upper opening place arranged transversely one trommel screen; The perforate of trommel screen end, is connected with the oil refining apparatus above end by pipeline, and the fuel reserve tank sidewall below trommel screen one end is provided with a power wheel, and described power wheel and roller grizzly pass through gear mesh; On described fuel reserve tank, be provided with a motor with the sidewall of power wheel homonymy, this motor is connected with power wheel by travelling belt.This kind of oil residue separating apparatus, simple to operate, easy to use, can manpower be saved, increase work efficiency and security, be applicable in animal grease treating processes being separated of oil and slag.
Patent 3:
Application number: 201420600173.2, the applying date: 2014-10-16, Shen Qing Publication day: 2015-02-11, the invention discloses a kind of extraction system proposing fat equipment and full-automation of animal oil, this carry fat equipment comprise have opening for feed, oil outlet, slag notch carry fat pot; Be positioned at and carry fat pot inner heating device; Be arranged on the stir shaft carried and arranging along himself short transverse in fat pot; Be fixedly installed on the blade on stir shaft; And the drive-motor for driving stir shaft to rotate, particularly, carry fat equipment also comprise the screen that is arranged on and carries and oil can be separated with the dregs of fat in fat pot and for separating of after the dregs of fat Residue extraction pipeline of discharging from slag notch and residual cake valve, wherein screen periphery and the inwall comprehensive engagement putting forward fat pot circumference, and screen is positioned at the below of blade.The utility model good mixing effect, reliability and stability are good and easy to maintenance.High, the basic non-environmental-pollution of oil yield of the utility model animal oil extraction system, labor strength are little, and meanwhile, structure is simple, and it is convenient, very practical to implement.
Found by above retrieval, above technical scheme can not affect novelty of the present invention; And the mutual combination of above patent document can not destroy creativeness of the present invention.
Summary of the invention
The object of this invention is to provide the treatment process of a kind of Non-intermittent formula commercial grease refinement and automatically refine system, adopt treatment process of the present invention and refinement system, the oil refining of Non-intermittent can be realized, control the temperature of extractive process different steps preferably simultaneously, improve the quality of oil refining, the dregs of fat and waste gas are all processed simultaneously, while environmental protection, also improve the utilization of the dregs of fat.
In order to realize above object, the technical solution used in the present invention is: the treatment process that a kind of Non-intermittent formula commercial grease refines, and it comprises the steps:
1., measure, the freezing raw material of animal tallow or fresh material are carried out Weighing through self-measuring device;
2., broken, the raw material that 1. step measures is transported in crusher through automatic transportation band and carries out fragmentation, and the raw material after fragmentation is the particle of diameter 8-12mm;
3., refine, the particulate material of step 2. after fragmentation is delivered in the extraction slot of device for refining through mass transport flood dragon, in extraction slot, front 30min is heating, the temperature of thermal oil is 220-260 DEG C, temperature of charge is made to rise to 150 DEG C, 30-60min is fuel-displaced, the temperature of thermal oil is 230-250 DEG C, temperature of charge is that 200 DEG C of beginnings are fuel-displaced in a large number, 60-90min is for boiling, temperature of charge controls at 150-170 DEG C, 90-120min is discharging, temperature of charge is 115-125 DEG C, mass transport is in next stage extraction slot, save extraction slot through 3-6 and repeat above-mentioned extractive process,
4., the dregs of fat are separated, the dregs of fat that 3. step extract enter into oil residue separating apparatus from dregs of fat outlet and carry out dregs of fat separation, the fluid part separated is delivered in first segment extraction slot by repairing pipe and is carried out repairing heating, and another part delivers to fluid hold tank after under meter metering;
5., squeeze, the dregs of fat that 4. step is separated are delivered to lard press through vertical flood dragon and are squeezed, and squeeze the fluid obtained and deliver to fluid hold tank after under meter metering, slag carries out filling bag through dregs of fat metering packaging machine and deposits;
6., gas sampling, 3. step is refined and collects through waste gas collection device with the waste gas that produces in step 4. dregs of fat separating step;
7., off gas treatment, by step 6. in the waste gas collected pass into emission-control equipment and carry out off gas treatment.
Preferably, step 2. in crusher comprise coarse breaking device and smart shredder assembly, broken particulate material diameter is out 10mm.
Preferably, step is 3. in extractive process, and in extraction slot, in front 30min, the temperature of thermal oil is 240 DEG C, and the temperature of 30-60min thermal 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, 3. in extractive process, have passed through 5 joint extraction slots and repeats to refine.
The automatic refinement system that a kind of Non-intermittent of another scheme of the present invention formula commercial grease refines, it comprises self-measuring device, described self-measuring device is connected to coarse breaking device by automatic transportation band, coarse breaking device is connected to smart shredder assembly, described smart shredder assembly is connected to device for refining by mass transport flood dragon, described device for refining is connected with oil residue separating apparatus, the oil outlet pipe (5) of described oil residue separating apparatus is connected to fluid hold tank and device for refining respectively by flow gauge and repairing pipe, the residue outlet (6) of oil residue separating apparatus is connected to lard press through vertical flood dragon, the oil outlet of described lard press is connected to fluid hold tank through flow gauge, slag notch is connected to dregs of fat metering packaging machine, described device for refining, oil residue separating apparatus and lard press are all connected with waste gas collection device, and waste gas collection device is connected to emission-control equipment, described self-measuring device, coarse breaking device, smart shredder assembly, device for refining, oil residue separating apparatus, lard press, waste gas collection device, emission-control equipment and dregs of fat metering packaging machine are all connected to automatic control system.
Further, described device for refining saves by 3-6 extraction slot (13) head and the tail tilted and is formed by connecting, and the discharge port of upper joint extraction slot (13) and the opening for feed docking of next joint extraction slot (13), the opening for feed of first segment extraction slot (13) is combined with feed-pipe (11), the discharge port of final section extraction slot (13) is dregs of fat outlet (1), the inside of described extraction slot (13) is provided with and pushes flood dragon (12), and outer cover adopts the heat-conducting layer (14) of thermal oil heat conduction; Described extraction slot (13) and heat-conducting layer (14) inside are provided with temperature inductor, and temperature inductor is connected with the electric temperature control valve in controller.
Further, described extraction slot (13) is round shape, and the inclined height of its end is not more than the radius of extraction slot (13).
Further, described oil residue separating apparatus comprise the dregs of fat outlet (1) below be tilted to the right arrange dregs of fat decoupled band (3), described dregs of fat decoupled band (3) is driven by the cylinder (2) of its inside; The below of described dregs of fat decoupled band (3) is provided with the separator tank (4) consistent with its obliquity, and the bottom left end of described separator tank (4) is provided with oil outlet pipe (5), bottom right-hand member is provided with residue outlet (6); It is characterized in that, rotating cylinder (9) is provided with in described separator tank (4), and the right-hand member of rotating cylinder (9) is connected on the motor (8) of separator tank (4) arranged outside, described rotating cylinder (9) is provided with screw-blade (10), and screw-blade (10) is positioned at immediately below dregs of fat outlet (1) and between residue outlet (6).
Further, the bottom interior surface of described separator tank (4) is provided with dividing plate (7), and be positioned on the left of the upper end of dividing plate (7) immediately below dregs of fat outlet (1) rightmost side on extended line, described rotating cylinder (9) is positioned between the right side wall of dividing plate (7) and separator tank (4).
Further, the lower portion oil filtering plate for oil (701) of described dividing plate (7); The outer rim position of described bolt blade (10) is oil strain layer (1001).
Beneficial effect of the present invention is:
1, technique of the present invention have employed full-automatic equipment, can realize the oil refining of Non-intermittent, controls the temperature of extractive process different steps simultaneously preferably, improves the quality of oil refining, prevents the situations such as fat burns and occurs.
2, all process the dregs of fat and waste gas in technique of the present invention, squeeze the dregs of fat, the fluid wherein do not refined can be squeezed out, the dregs of fat that simultaneously also can be left have carried out filling with bag and have utilized, and substantially increase economic benefit; Water vapor wherein can have been carried out recycle, without sewage discharge by exhaust collection and vent gas treatment, also protects environment simultaneously.
3, have employed more piece extraction slot in extractive process to repeat to refine, the oil yield of refinement can be improved, improve economical effectiveness.
4, device of the present invention have passed through controller whole-process control, achieves automated job, also can realize Non-intermittent operation simultaneously, substantially increase the efficiency of operation, reduces manpower work.
5, be provided with temperature sensor in extraction slot and in oil refining layer, and be connected to the temperature control valve in controller, extraction slot and the temperature in oil refining layer in each time period can well be controlled, ensure the stability of oil refining, substantially increase the quality of oil refining.
6, in the separator tank of oil residue separating apparatus, arrange one advance spiral flood dragon, the dregs of fat fallen in the middle part of decoupled band can be pushed to end through spiral flood dragon, and from the slag notch of end out, decrease the dregs of fat mixed volume in fluid, do not have the dregs of fat to deposit at separator tank simultaneously yet, therefore do not need cleaning, the continuous dregs of fat of Non-intermittent can be realized and be separated, be applicable to Non-intermittent grease frying production technique.
7, the design of dividing plate, can prevent the dregs of fat from entering into oil outlet pipe further, ensure that the fluid purity separated.
8, the oil filtering plate for oil design of the lower partition, it can only pass through fluid molecule, and not by the dregs of fat, and then the fluid that dregs of fat decoupled band can be made not separate enters into oil outlet pipe.
9, the oil strain layer of screw-blade peripheral edge portion can only pass through fluid molecule, and not by the dregs of fat, and then the fluid molecule of the omission that screw-blade can be advanced also can make it enter into oil outlet pipe, substantially increases the effect of separation.
Accompanying drawing explanation
Fig. 1 is the structural representation of the automatic refinement system that a kind of Non-intermittent formula commercial grease refines.
Fig. 2 is the structural representation of device for refining.
Fig. 3 is the structural representation of oil residue separating apparatus.
Fig. 4 is the partial enlarged drawing of A in Fig. 3.
Fig. 5 is the partial enlarged drawing of B in Fig. 3.
Shown in figure, label character is expressed as: 1, dregs of fat outlet; 2, cylinder; 3, dregs of fat decoupled band; 4, separator tank; 5, oil outlet pipe; 6, residue outlet; 7, dividing plate; 8, motor; 9, rotating cylinder; 10, screw-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.
Embodiment
In order to make those skilled in the art understand technical scheme of the present invention better, describe the present invention below in conjunction with accompanying drawing, the description of this part is only exemplary and explanatory, should not have any restriction to protection scope of the present invention.
As Figure 1-Figure 5, the automatic refinement system that a kind of Non-intermittent of the present invention formula commercial grease refines, it comprises self-measuring device, described self-measuring device is connected to coarse breaking device by automatic transportation band, coarse breaking device is connected to smart shredder assembly, described smart shredder assembly is connected to device for refining by mass transport flood dragon, described device for refining is connected with oil residue separating apparatus, the oil outlet pipe 5 of described oil residue separating apparatus is connected to fluid hold tank and device for refining respectively by flow gauge and repairing pipe, the residue outlet 6 of oil residue separating apparatus is connected to lard press through vertical flood dragon, the oil outlet of described lard press is connected to fluid hold tank through flow gauge, slag notch is connected to dregs of fat metering packaging machine, described device for refining, oil residue separating apparatus and lard press are all connected with waste gas collection device, and waste gas collection device is connected to emission-control equipment, described self-measuring device, coarse breaking device, smart shredder assembly, device for refining, oil residue separating apparatus, lard press, waste gas collection device, emission-control equipment and dregs of fat metering packaging machine are all connected to automatic control system.
Preferably, described device for refining saves by 3-6 extraction slot 13 head and the tail tilted and is formed by connecting, and the upper discharge port of a joint extraction slot 13 and the opening for feed docking of next joint extraction slot 13, the opening for feed of first segment extraction slot 13 is combined with feed-pipe 11, the discharge port of final section extraction slot 13 is dregs of fat outlet 1, the inside of described extraction slot 13 is provided with and pushes flood dragon 12, and outer cover adopts the heat-conducting layer 14 of thermal oil heat conduction; Described extraction slot 13 and heat-conducting layer 14 inside are provided with temperature inductor, and temperature inductor is connected with the electric temperature control valve in controller.
Preferably, described extraction slot 13 is round shape, and the inclined height of its end is not more than the radius of extraction slot 13.
Preferably, described oil residue separating apparatus comprise the dregs of fat outlet 1 below be tilted to the right arrange dregs of fat decoupled band 3, described dregs of fat decoupled band 3 is driven by the cylinder 2 of its inside; The below of described dregs of fat decoupled band 3 is provided with the separator tank 4 consistent with its obliquity, and the bottom left end of described separator tank 4 is provided with oil outlet pipe 5, bottom right-hand member is provided with residue outlet 6; It is characterized in that, in described separator tank 4, be provided with rotating cylinder 9, and the right-hand member of rotating cylinder 9 is connected on the motor 8 of separator tank 4 arranged outside, and described rotating cylinder 9 is provided with screw-blade 10, and screw-blade 10 is immediately below dregs of fat outlet 1 and between residue outlet 6.
Preferably, the bottom interior surface of described separator tank 4 is provided with dividing plate 7, and is positioned at the dregs of fat on the left of the upper end of dividing plate 7 and exports immediately below 1 rightmost side on extended line, described rotating cylinder 9 is between dividing plate 7 and the right side wall of separator tank 4.
Preferably, the lower portion oil filtering plate for oil 701 of described dividing plate 7; The outer rim position of described bolt blade 10 is oil strain layer 1001.
Wherein the work of oil residue separating apparatus is as follows: oil exports 1 out from the dregs of fat together with slag, drop on dregs of fat decoupled band 3 afterwards, fluid directly drops in separator tank 4 from the mesh dregs of fat decoupled band 3, and then go out from oil outlet pipe 5, the dregs of fat and a part of part can be travelled forward along with dregs of fat decoupled band 3 by the fluid that the dregs of fat block, the little dregs of fat of part and fluid can fall gradually along with the motion of dregs of fat decoupled band 3, the remaining dregs of fat can fall from the right-hand member of dregs of fat decoupled band 3, finally enter into residue outlet 6, and the fluid that middle part falls can enter into oil outlet pipe 5 through the oil filtering plate for oil 701 of the edge oil strain layer 1001 of screw-blade 10 and dividing plate 7 bottom, and the dregs of fat that middle part falls can finally enter into residue outlet 6 under the drive of screw-blade 10.
The embodiment of the treatment process adopting a kind of Non-intermittent formula commercial grease of aforesaid device to refine is as follows:
Embodiment 1
1., measure, the freezing raw material of animal tallow or fresh material are carried out Weighing through self-measuring device;
2., broken, the raw material that 1. step measures is transported in coarse breaking device and smart shredder assembly through automatic transportation band and carries out fragmentation, and the raw material after fragmentation is the particle of diameter 10mm;
3., refine, the particulate material of step 2. after fragmentation is delivered in the extraction slot of device for refining through mass transport flood dragon, in extraction slot, front 30min is heating, the temperature of thermal oil is 240 DEG C, temperature of charge is made to rise to 150 DEG C, 30-60min is fuel-displaced, and the temperature of thermal oil is 240 DEG C, and temperature of charge is that 200 DEG C of beginnings are fuel-displaced in a large number, 60-90min is for boiling, temperature of charge controls at 160 DEG C, and 90-120min is discharging, and temperature of charge is 120 DEG C, mass transport, in next stage extraction slot, repeats above-mentioned extractive process through 5 joint extraction slots;
4., the dregs of fat are separated, the dregs of fat that 3. step extract enter into oil residue separating apparatus from dregs of fat outlet and carry out dregs of fat separation, the fluid part separated is delivered in first segment extraction slot by repairing pipe and is carried out repairing heating, and another part delivers to fluid hold tank after under meter metering;
5., squeeze, the dregs of fat that 4. step is separated are delivered to lard press through vertical flood dragon and are squeezed, and squeeze the fluid obtained and deliver to fluid hold tank after under meter metering, slag carries out filling bag through dregs of fat metering packaging machine and deposits;
6., gas sampling, 3. step is refined and collects through waste gas collection device with the waste gas that produces in step 4. dregs of fat separating step;
7., off gas treatment, by step 6. in the waste gas collected pass into emission-control equipment and carry out off gas treatment.
Embodiment 2
1., measure, the freezing raw material of animal tallow or fresh material are carried out Weighing through self-measuring device;
2., broken, the raw material that 1. step measures is transported in coarse breaking device and smart shredder assembly through automatic transportation band and carries out fragmentation, and the raw material after fragmentation is the particle of diameter 8mm;
3., refine, the particulate material of step 2. after fragmentation is delivered in the extraction slot of device for refining through mass transport flood dragon, in extraction slot, front 30min is heating, the temperature of thermal oil is 260 DEG C, temperature of charge is made to rise to 150 DEG C, 30-60min is fuel-displaced, and the temperature of thermal oil is 230 DEG C, and temperature of charge is that 200 DEG C of beginnings are fuel-displaced in a large number, 60-90min is for boiling, temperature of charge controls at 170 DEG C, and 90-120min is discharging, and temperature of charge is 115 DEG C, mass transport, in next stage extraction slot, repeats above-mentioned extractive process through 3 joint extraction slots;
4., the dregs of fat are separated, the dregs of fat that 3. step extract enter into oil residue separating apparatus from dregs of fat outlet and carry out dregs of fat separation, the fluid part separated is delivered in first segment extraction slot by repairing pipe and is carried out repairing heating, and another part delivers to fluid hold tank after under meter metering;
5., squeeze, the dregs of fat that 4. step is separated are delivered to lard press through vertical flood dragon and are squeezed, and squeeze the fluid obtained and deliver to fluid hold tank after under meter metering, slag carries out filling bag through dregs of fat metering packaging machine and deposits;
6., gas sampling, 3. step is refined and collects through waste gas collection device with the waste gas that produces in step 4. dregs of fat separating step;
7., off gas treatment, by step 6. in the waste gas collected pass into emission-control equipment and carry out off gas treatment.
Embodiment 3
1., measure, the freezing raw material of animal tallow or fresh material are carried out Weighing through self-measuring device;
2., broken, the raw material that 1. step measures is transported in coarse breaking device and smart shredder assembly through automatic transportation band and carries out fragmentation, and the raw material after fragmentation is the particle of diameter 12mm;
3., refine, the particulate material of step 2. after fragmentation is delivered in the extraction slot of device for refining through mass transport flood dragon, in extraction slot, front 30min is heating, the temperature of thermal oil is 220 DEG C, temperature of charge is made to rise to 150 DEG C, 30-60min is fuel-displaced, and the temperature of thermal oil is 250 DEG C, and temperature of charge is that 200 DEG C of beginnings are fuel-displaced in a large number, 60-90min is for boiling, temperature of charge controls at 150 DEG C, and 90-120min is discharging, and temperature of charge is 125 DEG C, mass transport, in next stage extraction slot, repeats above-mentioned extractive process through 6 joint extraction slots;
4., the dregs of fat are separated, the dregs of fat that 3. step extract enter into oil residue separating apparatus from dregs of fat outlet and carry out dregs of fat separation, the fluid part separated is delivered in first segment extraction slot by repairing pipe and is carried out repairing heating, and another part delivers to fluid hold tank after under meter metering;
5., squeeze, the dregs of fat that 4. step is separated are delivered to lard press through vertical flood dragon and are squeezed, and squeeze the fluid obtained and deliver to fluid hold tank after under meter metering, slag carries out filling bag through dregs of fat metering packaging machine and deposits;
6., gas sampling, 3. step is refined and collects through waste gas collection device with the waste gas that produces in step 4. dregs of fat separating step;
7., off gas treatment, by step 6. in the waste gas collected pass into emission-control equipment and carry out off gas treatment.
It should be noted that, in this article, term " comprises ", " comprising " or its any other variant are intended to contain comprising of nonexcludability, thus make to comprise the process of a series of key element, method, article or equipment and not only comprise which key element, but also comprise other key elements clearly do not listed, or also comprise by the intrinsic key element of this process, method, article or equipment.
Apply specific case herein to set forth principle of the present invention and embodiment, the explanation of above example just understands method of the present invention and core concept thereof for helping.The above is only the preferred embodiment of the present invention, should be understood that, due to the finiteness of literal expression, and objectively there is unlimited concrete structure, for those skilled in the art, under the premise without departing from the principles of the invention, some improvement, retouching or change can also be made, also above-mentioned technical characteristic can be combined by rights; These improve retouching, change or combination, or the design of invention and technical scheme are directly applied to other occasion without improving, and all should be considered as protection scope of the present invention.
Claims (10)
1. a treatment process for Non-intermittent formula commercial grease refinement, it is characterized in that, it comprises the steps:
1., measure, the freezing raw material of animal tallow or fresh material are carried out Weighing through self-measuring device;
2., broken, the raw material that 1. step measures is transported in crusher through automatic transportation band and carries out fragmentation, and the raw material after fragmentation is the particle of diameter 8-12mm;
3., refine, the particulate material of step 2. after fragmentation is delivered in the extraction slot of device for refining through mass transport flood dragon, in extraction slot, front 30min is heating, the temperature of thermal oil is 220-260 DEG C, temperature of charge is made to rise to 150 DEG C, 30-60min is fuel-displaced, the temperature of thermal oil is 230-250 DEG C, temperature of charge is that 200 DEG C of beginnings are fuel-displaced in a large number, 60-90min is for boiling, temperature of charge controls at 150-170 DEG C, 90-120min is discharging, temperature of charge is 115-125 DEG C, mass transport is in next stage extraction slot, save extraction slot through 3-6 and repeat above-mentioned extractive process,
4., the dregs of fat are separated, the dregs of fat that 3. step extract enter into oil residue separating apparatus from dregs of fat outlet and carry out dregs of fat separation, the fluid part separated is delivered in first segment extraction slot by repairing pipe and is carried out repairing heating, and another part delivers to fluid hold tank after under meter metering;
5., squeeze, the dregs of fat that 4. step is separated are delivered to lard press through vertical flood dragon and are squeezed, and squeeze the fluid obtained and deliver to fluid hold tank after under meter metering, slag carries out filling bag through dregs of fat metering packaging machine and deposits;
6., gas sampling, 3. step is refined and collects through waste gas collection device with the waste gas that produces in step 4. dregs of fat separating step;
7., off gas treatment, by step 6. in the waste gas collected pass into emission-control equipment and carry out off gas treatment.
2. the treatment process that refines of a kind of Non-intermittent formula commercial grease according to claim 1, is characterized in that, step 2. in crusher comprise coarse breaking device and smart shredder assembly, broken particulate material diameter is out 10mm.
3. the treatment process of a kind of Non-intermittent formula commercial grease refinement according to claim 1, it is characterized in that, step is 3. in extractive process, in extraction slot, in front 30min, the temperature of thermal oil is 240 DEG C, the temperature of 30-60min thermal 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.
4. the treatment process that refines of a kind of Non-intermittent formula commercial grease according to claim 3, is characterized in that, step, 3. in extractive process, have passed through 5 joint extraction slots and repeats to refine.
5. as any one of claim 1-4 treatment process a kind of Non-intermittent formula commercial grease that the adopts automatic refinement system of refining, it is characterized in that, it comprises self-measuring device, described self-measuring device is connected to coarse breaking device by automatic transportation band, coarse breaking device is connected to smart shredder assembly, described smart shredder assembly is connected to device for refining by mass transport flood dragon, described device for refining is connected with oil residue separating apparatus, the oil outlet pipe (5) of described oil residue separating apparatus is connected to fluid hold tank and device for refining respectively by flow gauge and repairing pipe, the residue outlet (6) of oil residue separating apparatus is connected to lard press through vertical flood dragon, the oil outlet of described lard press is connected to fluid hold tank through flow gauge, slag notch is connected to dregs of fat metering packaging machine, described device for refining, oil residue separating apparatus and lard press are all connected with waste gas collection device, and waste gas collection device is connected to emission-control equipment, described self-measuring device, coarse breaking device, smart shredder assembly, device for refining, oil residue separating apparatus, lard press, waste gas collection device, emission-control equipment and dregs of fat metering packaging machine are all connected to automatic control system.
6. the automatic refinement system of a kind of Non-intermittent formula commercial grease refinement according to claim 5, it is characterized in that, described device for refining saves by 3-6 extraction slot (13) head and the tail tilted and is formed by connecting, and the discharge port of upper joint extraction slot (13) and the opening for feed docking of next joint extraction slot (13), the opening for feed of first segment extraction slot (13) is combined with feed-pipe (11), the discharge port of final section extraction slot (13) is dregs of fat outlet (1), the inside of described extraction slot (13) is provided with and pushes flood dragon (12), outer cover adopts the heat-conducting layer (14) of thermal oil heat conduction, described extraction slot (13) and heat-conducting layer (14) inside are provided with temperature inductor, and temperature inductor is connected with the electric temperature control valve in controller.
7. the automatic refinement system of a kind of Non-intermittent formula commercial grease refinement according to claim 6, it is characterized in that, described extraction slot (13) is round shape, and the inclined height of its end is not more than the radius of extraction slot (13).
8. the automatic refinement system of a kind of Non-intermittent formula commercial grease refinement according to claim 6, it is characterized in that, described oil residue separating apparatus comprise the dregs of fat outlet (1) below be tilted to the right arrange dregs of fat decoupled band (3), described dregs of fat decoupled band (3) is driven by the cylinder (2) of its inside; The below of described dregs of fat decoupled band (3) is provided with the separator tank (4) consistent with its obliquity, and the bottom left end of described separator tank (4) is provided with oil outlet pipe (5), bottom right-hand member is provided with residue outlet (6); It is characterized in that, rotating cylinder (9) is provided with in described separator tank (4), and the right-hand member of rotating cylinder (9) is connected on the motor (8) of separator tank (4) arranged outside, described rotating cylinder (9) is provided with screw-blade (10), and screw-blade (10) is positioned at immediately below dregs of fat outlet (1) and between residue outlet (6).
9. the automatic refinement system of a kind of Non-intermittent formula commercial grease refinement according to claim 8, it is characterized in that, the bottom interior surface of described separator tank (4) is provided with dividing plate (7), and be positioned on the left of the upper end of dividing plate (7) immediately below dregs of fat outlet (1) rightmost side on extended line, described rotating cylinder (9) is positioned between the right side wall of dividing plate (7) and separator tank (4).
10. the automatic refinement system of a kind of Non-intermittent formula commercial grease refinement according to claim 9, is characterized in that, the lower portion oil filtering plate for oil (701) of described dividing plate (7); The outer rim position of described bolt blade (10) is oil strain layer (1001).
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| CN112536311A (en) * | 2020-11-19 | 2021-03-23 | 湖南祥柏生态环保科技有限公司 | Energy-saving environment-friendly comprehensive system for innocent treatment of animals died of diseases |
| CN113828193A (en) * | 2021-09-23 | 2021-12-24 | 江苏德康医疗器械有限公司 | Mink oil extraction element for cosmetics |
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