CN110499244A - A kind of emulsification glycolysis device and emulsification glycolysis method - Google Patents
A kind of emulsification glycolysis device and emulsification glycolysis method Download PDFInfo
- Publication number
- CN110499244A CN110499244A CN201910661423.0A CN201910661423A CN110499244A CN 110499244 A CN110499244 A CN 110499244A CN 201910661423 A CN201910661423 A CN 201910661423A CN 110499244 A CN110499244 A CN 110499244A
- Authority
- CN
- China
- Prior art keywords
- emulsification
- glycolysis
- tank body
- tank
- fermentor
- 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.)
- Pending
Links
- 238000004945 emulsification Methods 0.000 title claims abstract description 98
- 230000034659 glycolysis Effects 0.000 title claims abstract description 55
- 238000000034 method Methods 0.000 title claims abstract description 16
- 238000012545 processing Methods 0.000 claims abstract description 35
- 238000003756 stirring Methods 0.000 claims abstract description 32
- 230000001954 sterilising effect Effects 0.000 claims abstract description 31
- 238000000855 fermentation Methods 0.000 claims abstract description 24
- 238000010564 aerobic fermentation Methods 0.000 claims abstract description 23
- 239000003995 emulsifying agent Substances 0.000 claims abstract description 22
- 238000004519 manufacturing process Methods 0.000 claims abstract description 11
- 239000003638 chemical reducing agent Substances 0.000 claims abstract description 8
- 230000001580 bacterial effect Effects 0.000 claims abstract description 6
- 235000013622 meat product Nutrition 0.000 claims abstract description 6
- 229910001220 stainless steel Inorganic materials 0.000 claims abstract description 6
- 239000010935 stainless steel Substances 0.000 claims abstract description 6
- 230000001804 emulsifying effect Effects 0.000 claims abstract description 5
- 210000003608 fece Anatomy 0.000 claims abstract description 5
- 239000010871 livestock manure Substances 0.000 claims abstract description 5
- 244000005700 microbiome Species 0.000 claims abstract description 4
- 230000002093 peripheral effect Effects 0.000 claims abstract description 4
- 230000002906 microbiologic effect Effects 0.000 claims abstract 2
- 239000000463 material Substances 0.000 claims description 46
- 239000002068 microbial inoculum Substances 0.000 claims description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 16
- 238000002156 mixing Methods 0.000 claims description 14
- 230000005540 biological transmission Effects 0.000 claims description 12
- 238000010438 heat treatment Methods 0.000 claims description 10
- 241000222120 Candida <Saccharomycetales> Species 0.000 claims description 9
- 240000001046 Lactobacillus acidophilus Species 0.000 claims description 9
- 235000013956 Lactobacillus acidophilus Nutrition 0.000 claims description 9
- 240000006024 Lactobacillus plantarum Species 0.000 claims description 9
- 235000013965 Lactobacillus plantarum Nutrition 0.000 claims description 9
- 240000004808 Saccharomyces cerevisiae Species 0.000 claims description 9
- 235000014680 Saccharomyces cerevisiae Nutrition 0.000 claims description 9
- 239000007789 gas Substances 0.000 claims description 9
- 239000008236 heating water Substances 0.000 claims description 9
- 229940039695 lactobacillus acidophilus Drugs 0.000 claims description 9
- 229940072205 lactobacillus plantarum Drugs 0.000 claims description 9
- 244000063299 Bacillus subtilis Species 0.000 claims description 8
- 235000014469 Bacillus subtilis Nutrition 0.000 claims description 8
- 241000894006 Bacteria Species 0.000 claims description 8
- 241000194032 Enterococcus faecalis Species 0.000 claims description 8
- 102000004190 Enzymes Human genes 0.000 claims description 8
- 108090000790 Enzymes Proteins 0.000 claims description 8
- 102000004882 Lipase Human genes 0.000 claims description 8
- 108090001060 Lipase Proteins 0.000 claims description 8
- 239000004367 Lipase Substances 0.000 claims description 8
- 101000693530 Staphylococcus aureus Staphylokinase Proteins 0.000 claims description 8
- 229940032049 enterococcus faecalis Drugs 0.000 claims description 8
- 235000019421 lipase Nutrition 0.000 claims description 8
- 230000007935 neutral effect Effects 0.000 claims description 8
- 238000011282 treatment Methods 0.000 claims description 8
- 241000228212 Aspergillus Species 0.000 claims description 7
- 238000001816 cooling Methods 0.000 claims description 7
- 230000003247 decreasing effect Effects 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 5
- 238000009472 formulation Methods 0.000 claims description 4
- 239000001301 oxygen Substances 0.000 claims description 2
- 229910052760 oxygen Inorganic materials 0.000 claims description 2
- 239000006071 cream Substances 0.000 claims 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims 1
- 239000000047 product Substances 0.000 description 32
- 239000006227 byproduct Substances 0.000 description 16
- 241000287828 Gallus gallus Species 0.000 description 11
- 235000013330 chicken meat Nutrition 0.000 description 11
- 235000013372 meat Nutrition 0.000 description 11
- 235000013305 food Nutrition 0.000 description 8
- 230000004151 fermentation Effects 0.000 description 7
- 210000000936 intestine Anatomy 0.000 description 6
- 230000009965 odorless effect Effects 0.000 description 6
- 239000002304 perfume Substances 0.000 description 6
- 238000002360 preparation method Methods 0.000 description 6
- 238000003860 storage Methods 0.000 description 6
- 235000012055 fruits and vegetables Nutrition 0.000 description 5
- 150000001413 amino acids Chemical class 0.000 description 4
- 210000000988 bone and bone Anatomy 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 108090000765 processed proteins & peptides Proteins 0.000 description 4
- 238000003307 slaughter Methods 0.000 description 4
- 244000046052 Phaseolus vulgaris Species 0.000 description 3
- 235000010627 Phaseolus vulgaris Nutrition 0.000 description 3
- 239000003814 drug Substances 0.000 description 3
- 230000007071 enzymatic hydrolysis Effects 0.000 description 3
- 238000006047 enzymatic hydrolysis reaction Methods 0.000 description 3
- 238000012856 packing Methods 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 241001465754 Metazoa Species 0.000 description 2
- 210000004027 cell Anatomy 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000839 emulsion Substances 0.000 description 2
- 239000003337 fertilizer Substances 0.000 description 2
- 230000010354 integration Effects 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 244000144977 poultry Species 0.000 description 2
- 235000013594 poultry meat Nutrition 0.000 description 2
- 239000007790 solid phase Substances 0.000 description 2
- 238000004659 sterilization and disinfection Methods 0.000 description 2
- 241000251468 Actinopterygii Species 0.000 description 1
- 241000193830 Bacillus <bacterium> Species 0.000 description 1
- 241000283690 Bos taurus Species 0.000 description 1
- 244000025254 Cannabis sativa Species 0.000 description 1
- 241000726221 Gemma Species 0.000 description 1
- 108010038807 Oligopeptides Proteins 0.000 description 1
- 102000015636 Oligopeptides Human genes 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 241001494479 Pecora Species 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 239000002518 antifoaming agent Substances 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009933 burial Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 230000012447 hatching Effects 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 238000011081 inoculation Methods 0.000 description 1
- 239000012774 insulation material Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 230000004060 metabolic process Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 229920001542 oligosaccharide Polymers 0.000 description 1
- 150000002482 oligosaccharides Chemical class 0.000 description 1
- 244000052769 pathogen Species 0.000 description 1
- 230000001717 pathogenic effect Effects 0.000 description 1
- 210000002381 plasma Anatomy 0.000 description 1
- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 238000009738 saturating Methods 0.000 description 1
- 235000015067 sauces Nutrition 0.000 description 1
- 230000011218 segmentation Effects 0.000 description 1
- 230000003319 supportive effect Effects 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 230000014621 translational initiation Effects 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L13/00—Meat products; Meat meal; Preparation or treatment thereof
- A23L13/40—Meat products; Meat meal; Preparation or treatment thereof containing additives
- A23L13/45—Addition of, or treatment with, microorganisms
- A23L13/46—Addition of, or fermentation with fungi, e.g. yeasts; Enrichment with dried biomass other than starter cultures
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L13/00—Meat products; Meat meal; Preparation or treatment thereof
- A23L13/40—Meat products; Meat meal; Preparation or treatment thereof containing additives
- A23L13/48—Addition of, or treatment with, enzymes
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L17/00—Food-from-the-sea products; Fish products; Fish meal; Fish-egg substitutes; Preparation or treatment thereof
- A23L17/65—Addition of, or treatment with, microorganisms or enzymes
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23N—MACHINES OR APPARATUS FOR TREATING HARVESTED FRUIT, VEGETABLES OR FLOWER BULBS IN BULK, NOT OTHERWISE PROVIDED FOR; PEELING VEGETABLES OR FRUIT IN BULK; APPARATUS FOR PREPARING ANIMAL FEEDING- STUFFS
- A23N17/00—Apparatus specially adapted for preparing animal feeding-stuffs
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F1/00—Fertilisers made from animal corpses, or parts thereof
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F11/00—Other organic fertilisers
- C05F11/08—Organic fertilisers containing added bacterial cultures, mycelia or the like
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M21/00—Bioreactors or fermenters specially adapted for specific uses
- C12M21/18—Apparatus specially designed for the use of free, immobilized or carrier-bound enzymes
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/02—Form or structure of the vessel
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M27/00—Means for mixing, agitating or circulating fluids in the vessel
- C12M27/02—Stirrer or mobile mixing elements
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/20—Degassing; Venting; Bubble traps
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M33/00—Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus
- C12M33/04—Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus by injection or suction, e.g. using pipettes, syringes, needles
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/12—Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M45/00—Means for pre-treatment of biological substances
- C12M45/02—Means for pre-treatment of biological substances by mechanical forces; Stirring; Trituration; Comminuting
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M45/00—Means for pre-treatment of biological substances
- C12M45/20—Heating; Cooling
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Zoology (AREA)
- Wood Science & Technology (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Microbiology (AREA)
- Sustainable Development (AREA)
- Biotechnology (AREA)
- Genetics & Genomics (AREA)
- Biochemistry (AREA)
- General Health & Medical Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Biomedical Technology (AREA)
- Molecular Biology (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Nutrition Science (AREA)
- Clinical Laboratory Science (AREA)
- Mycology (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Analytical Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Marine Sciences & Fisheries (AREA)
- Mechanical Engineering (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
The invention discloses a kind of emulsification glycolysis devices, and including emulsification fermentor and the pulverizer being disposed thereon, the discharge port of pulverizer is communicated to the feed inlet of emulsification fermentor；Emulsifying fermentor includes tank body, and tank body peripheral wall is made of double-layer stainless steel, and circulating coil is welded on inner wall；Tank interior is additionally provided with agitating device and emulsifier unit, agitating device includes the stirring motor for being provided with tank deck, and stirring motor lower part is connected with speed reducer, and speed reducer lower part is connected with agitating shaft, agitating shaft top is equipped with defoaming rake, is provided with 5~8 stirring blades at shaft bottom port；Air inlet, gas outlet are additionally provided on tank body；The method and other application using device emulsification glycolysis are also disclosed simultaneously.Of the invention can successively realize the processing such as comminuting matter, emulsification sterilizing, aerobic fermentation, anaerobic fermentation；Meat product deep processing, deep processing of farm products, microbiological feed production and the production of agricultural microorganism bacterial manure can be widely used in.
Description
Technical field
The present invention relates to technical field of bioengineering more particularly to a kind of emulsification glycolysis device and emulsification glycolysis methods.
Background technique
China is maximum meat production and country of consumption in the world, the annual processing of farm products for generating more than 1,800 ten thousand tons and poultry
Fowl butchers byproduct, for these processings of farm products and animal by-products, in addition to be used on a small quantity biochemical pharmacy, the raw material of industry and
Feedstuff, major part is directly burned, burial is handled.Such as slaughtering chickens intestines, in addition to being eaten a little by the mankind, big department is direct
It is as aquatic feed or directly discarded, cause the wasting of resources, environmental pollution and transmission problem；Pig bone and cattle and sheep bone, with
And chicken carcasses, it is most of because being utilized without suitable digestion approach without being integrated into.It can be seen that animality byproduct is not
The development trend come undergoes technological transformation to slaughtering by-product process systems with applicating modern times technology and equipment, to provide
The product of more high-quality and safety is attached most importance to, and utilizes food processing or slaughtering processed side product in processing efficiently.
Relevant in the prior art in slaughtering, CN201610708893.4 discloses one kind and adds suitable for meat production
The large-scale meat grinder of work enterprise, including Minced Steak box body, meat grinder lower bottom base, meat grinder cage can be used for meat products processing,
But it is only that meat products is carried out rubbing processing.CN201711234287.4 disclose one kind to vacuumize as power source,
Chicken intestines are sucked in outer tube, the device of cutting pre-cleaning is carried out by the cooperation of cutter and internal lining pipe, also only for
It is the pretreatment of chicken intestines, food production is used for after processing.
Although CN201820401011.4 discloses a kind of efficient emulsifying machine agitator tank, including mulser agitator tank ontology,
Motor, supporting leg, infrared heating device, universal wheel, manhole, insulating layer, discharge port and control cabinet, can efficiently stirring when into
Row heating.But this patent does not disclose the overall plan for butchering by-product processing yet, therefore can not realize to butchering pair
The processing of product high value-added.
Correspondingly, some agricultural product or processing of farm products by-product are also required to carry out high value-added processing, to obtain more
High profit.
Summary of the invention
The first technical problem to be solved by the present invention is: providing a kind of emulsification glycolysis device, which be can be realized
Pyrohydrolysis, emulsification broken wall, biological glycolysis triple effect cooperated integration function, and high-temperature sterilization, medium temperature enzymatic hydrolysis, normal temperature fermentation three are closed
One integrated function.
Second technical problem to be solved by this invention is: providing a kind of above-mentioned emulsification glycolysis device of utilization and handles meat
And its method of processed side product, material can be crushed, be emulsified, being sterilized by this method, glycolysis, and it is raw to be translated into function
Object peptide ferment.
The present invention also provides the applications of the emulsification glycolysis device.
In order to solve the above technical problems, the technical scheme is that
A kind of emulsification glycolysis device, including emulsification glycolysis tank and the pulverizer being disposed thereon, the discharge port of pulverizer connects
Lead to the feed inlet of emulsification glycolysis tank；
Emulsification glycolysis tank includes tank body, and the top of tank body is equipped with feed inlet, and bottom is equipped with discharge port；Tank body peripheral wall is by bilayer
Stainless steel forms, and is welded with circulating coil on internal layer inner wall；Tank interior is additionally provided with agitating device and emulsifier unit, stirring dress
The stirring motor including being provided with tank deck is set, stirring motor lower part is connected with speed reducer, and speed reducer lower part is connected with agitating shaft, stirs
It mixes axis top and is equipped with defoaming rake, be provided with 5~8 stirring blades at shaft bottom port；Air inlet is additionally provided on tank body
The gas outlet and.
Preferably, the circulating coil is connected to external heating water tank, and realizes hot water circulation heated by circulating pump
Function.More than one temperature sensor is additionally provided in tank body, circulating pump and temperature sensor are all connected to automatic control system.
Preferably, the emulsifier unit is set to tank base, including the emulsification motor being set on the outside of tank base,
It emulsifies motor top and is equipped with transmission shaft, transmission shaft is entered across tank body and is set to inside the frame housing of tank base；Emulsification
The bottom of the frame of device is closed disk, and disk top is fixedly connected with the shell of circular hollow, lower part of the housing setting upwards
There is more than one hollow out mouth (saturating material mouth), upper part of the housing is arranged in parallel with several grooves；It is set on the transmission shaft of enclosure interior
It is equipped with agitating paddle.
Further, several grooves of the upper part of the housing are oblique parallel setting.
Preferably, thermal insulation material is full of between the emulsification glycolysis tank outer layer stainless steel and internal layer stainless steel.
Preferably, defoaming rake lower part is provided with more than one defoaming tooth.
Preferably, the stirring motor and emulsification motor are all connected to automatic control system.
Preferably, the pulverizer is that extra large day freezes meat grinder, and manufacturer is that day aquatic products food machinery in Qingdao sea adds
Factory.
Preferably, the external air compressor of the air inlet, and by setting air inlet frequency, and realize Aerobic-anaerobic-
Aerobic alternating ferment control, to achieve the purpose that the double dynamic fermentations of solid phase.
Preferably, the surrounding of the emulsification glycolysis device and bottom are provided with frame body, to emulsification glycolysis tank and pulverizer
Play support and protective effect.
Utilize the method for above-mentioned emulsification glycolysis device emulsification glycolysis, comprising the following steps:
A. material is cleaned and (is first thawed if it is the material of frost processing), be then lifted out investment pulverizer
In, it opens pulverizer and carries out pre- rubbing processing；
B. the material after rubbing is sent into the fermentor for being set to and rubbing motor spindle, and proper amount of clear water is added (to flood emulsification
The rack of device is advisable), open heating water bath, emulsifier unit (revolving speed 1400r/min) and agitating device (revolving speed is 200~
300r/min), sterilizing emulsification treatment is carried out to material, when material temperature reaches 80 DEG C or so, stops heating and insulated sterilizing 30 divides
It is more than clock；
C. after the completion of material sterilizing emulsification, emulsifier unit is closed, circulating water cooling and agitating device (revolving speed 200 are opened
~300r/min), when material temperature being made to be gradually decreased to 35 DEG C or so, put into the aerobic fermentation microbial inoculum of 1% mass ratio, including withered grass gemma
Bacillus: saccharomyces cerevisiae: produce gastral cavity Candida: Aspergillus is cooperated by the mass ratio of 1:2:1:1:0.5, puts into 0.1%
Complex enzyme formulation, including neutral proteinase: neutral lipase is cooperated by 1:1 mass ratio；It is then turned on emulsification, mixing dress
It sets and carries out fully emulsified mixing 30 minutes；
D. after sterilizing emulsification, every 30min stirring gas supply 10min is set, ferments 24 hours in 30~35 DEG C, carries out aerobic hair
Ferment；
E. aerobic fermentation terminates, and anaerobic fermentation microbial inoculum, including lactobacillus plantarum is added: enterococcus faecalis: lactobacillus acidophilus is pressed
The mass ratio of 1:2:1 cooperates, and is uniformly mixed, and self-controlled circulating 10min/3h is arranged, in 30~35 DEG C of fermentations 24
Hour, carry out anaerobism flavouring；
F. product after anaerobic fermentation is odorless, micro-perfume, the product after being processed；The product can be further processed
Other products are prepared, or keeps in and carries out storing in sealed storage tank for use.
Preferably, the revolving speed of the emulsification in the step b is 1400rpm；The revolving speed of stirring be 200rpm extremely
300rpm。
Preferably, the revolving speed stirred in the step c is 200rpm to 300rpm；Bacillus subtilis, saccharomyces cerevisiae
It is respectively 1.0~5.0 × 10 with the viable count for producing gastral cavity Candida8It is a；Neutral proteinase has purchased from the road Dong Henghua biotechnology
Responsible company is limited, neutral lipase believes Chemical Co., Ltd. purchased from Chengdu ten thousand.
Preferably, the revolving speed stirred in the step d is 200rpm to 300rpm；Oxygen-supplying amount is 1.6M3/min。
Preferably, the revolving speed of the stirring in the step e is 200rpm to 300rpm；Lactobacillus plantarum: excrement intestines ball
Bacterium: every gram of viable count of lactobacillus acidophilus is respectively 1.0~5.0 × 108It is a.
Emulsify the application of glycolysis device: the emulsification glycolysis device is in meat product deep processing, deep processing of farm products, microorganism
Application in Feed Manufacturing and the production of agricultural microorganism bacterial manure.Wherein: preparing functional amino using meat, pig bone, chicken bone
Enzyme food；Functional fish sauce ferment conditioning food is prepared using aquatic products；It is made using source property Chinese medicine (containing dark green Chinese medicine) is planted
Standby Chinese medicine ferment；Functional garden stuff enzyme food is prepared using water fruits and vegetables；Functional beans peptide ferment is prepared using beans agricultural product
Vegetable food；Functional egg peptide enzyme food is prepared using egg；Using butchering by-product chicken intestines, blood plasma, pluck, aquatic products processing
By-product prepares function amino acid ferment raw material；Function amino acid ferment raw material is prepared using dregs of beans, miscellaneous dregs of rice；Using fruits and vegetables and its
Processing byproduct prepares functional ferment fertilizer；Function amino acid ferment is prepared using animals died of illness, scrambled egg, the residual young, afterbirth of hatching
Plain bacterial manure.
By adopting the above-described technical solution, the beneficial effects of the present invention are:
1, the present invention has pyrohydrolysis, emulsification broken wall, biological glycolysis triple effect cooperated integration technology, it is only necessary to 30 minutes
Breaking-wall cell and biological depolymerization function can be realized, and emulsion form nutriment is made after depolymerization to reach efficient with functional microbial
Interaction dissolves affinity state.
2, the present invention was being sterilized using " high-temperature sterilization, medium temperature enzymatic hydrolysis, normal temperature fermentation " three-in-one integrated function, material
In journey cell expanded by heating and rapidly by broken wall emulsification be emulsion liquid, can not only kill pathogen, but also can effectively protect material air
Taste nutrient.Segmentation inoculation complex enzyme formulation and microbial bacterial agent in temperature-fall period, to realize that the collaboration of bacterium-enzyme promotes
Function.
3, the present invention utilizes " triple effect depolymerization and biopolymerization " integrated function, is inoculated with life by the material after disaggregation processing
Object fermenting agent can be directed to metabolism and generate oligopeptides, oligosaccharides, small peptide, amino acid, fatty acid and other functional components.
4, present device use integrated automatic control system, it can be achieved that temperature control, oxygen supply, stirring, emulsification pretreatment etc. from
Dynamic control function can meet the efficient enzymatic hydrolysis of material, aerobic fermentation, limit a variety of enzymes such as the double dynamic equilibrium fermentations of aerobe fermentation, solid phase
The requirement of hydrolysis and fermentation process conditions.
5, defoaming of the invention rake and defoaming tooth can eliminate the foam generated in production process, in order to avoid addition defoaming agent pair
Production has an adverse effect；Emulsifier unit is provided with agitating paddle and can be stirred to material, and the material moved after stirring passes through
It is fully emulsified after specially designed hollow out mouth and groove, reach preset emulsifying effectiveness.
In short, the device of the invention can successively realize the processing such as comminuting matter, emulsification sterilizing, biological glycolysis；It can be extensive
Be applied to the agricultures such as meat product and its efficient enzymolysis processing of by-product, aquatic products and its efficient glycolysis processing of by-product, fruits and vegetables
The efficient glycolysis processing of product；And 50 jin or less dead livestock and poultry harmless treatments.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the embodiment of the present invention；
Fig. 2 is the structural schematic diagram of rack and section transmission axis in emulsification glycolysis tank of the embodiment of the present invention；
In figure, 1- emulsifies glycolysis tank；2- pulverizer；3- tank body；4- feed inlet；5- discharge port；6- circulating coil；7- stirring
Device；71- stirring motor；72- speed reducer；73- agitating shaft；74- defoaming rake；75- stirring blade；76- defoams tooth；8- emulsification dress
It sets；81- emulsifies motor；82- transmission shaft；83- rack；831- disk；832- shell；833- hollow out mouth；834- groove；84- is stirred
Mix paddle.
Specific embodiment
With reference to the accompanying drawings and examples, the present invention is further explained.
Embodiment one: emulsification glycolysis device
As depicted in figs. 1 and 2, glycolysis device is emulsified, including emulsification glycolysis tank 1 and the pulverizer 2 being disposed thereon, is rubbed
The discharge port (not shown) of machine 2 is communicated to the feed inlet 4 of emulsification glycolysis tank 1.
Emulsifying glycolysis tank 1 includes tank body 3, and the top of tank body 3 is equipped with feed inlet 4, and bottom is equipped with discharge port 5；3 peripheral wall of tank body
It is made of double-layer stainless steel, circulating coil 6 is welded on internal layer inner wall, be additionally provided with more than one temperature sensor and (do not mark
Out)；Agitating device 7 and emulsifier unit 8 are additionally provided with inside tank body 3, agitating device 7 includes the stirring motor for being provided with tank deck
71,71 lower part of stirring motor is connected with speed reducer 72, and 72 lower part of speed reducer is connected with agitating shaft 73, and 73 top of agitating shaft, which is equipped with, to disappear
Bubble rake 74, defoaming rake lower part are provided with more than one defoaming tooth 76,6 stirring blades are provided at 73 bottom port of agitating shaft
75；Air inlet (not shown), gas outlet (not shown) are additionally provided on tank body 3.
Emulsifier unit 8 is set to 3 bottom of tank body, the emulsification motor 81 including being set to 3 bottom outside of tank body, emulsifies motor
81 tops are equipped with transmission shaft 82, and transmission shaft 82 passes through tank body 3 and enters in the shell 832 for the rack 83 for being set to 3 bottom of tank body
Portion；83 bottom of rack of emulsifier unit 8 is closed disk 831, and 831 top of disk is fixedly connected with the shell of circular hollow upwards
Body 832,832 lower part of shell are provided with more than one hollow out mouth 833, and shell 832 is upper parallel to be provided with several grooves 834；Position
Agitating paddle 84 is provided on transmission shaft 82 inside shell 832.
Embodiment two: the method one of emulsification glycolysis device emulsification glycolysis processing meat packing by-product:
A. chicken intestines thawed, cleaned, is then lifted out in investment pulverizer, opened pulverizer and carry out pre- rubbing processing；
B. the material after rubbing is sent into the fermentor for being set to and rubbing motor spindle, and proper amount of clear water is added (to flood emulsification
The rack of device is advisable), open heating water bath, emulsifier unit (revolving speed 1400r/min) and agitating device (revolving speed 200r/
Min), sterilizing emulsification treatment is carried out to material, when material temperature reaches 80 DEG C or so, stop heating and insulated sterilizing 30 minutes with
On；
C. after the completion of material sterilizing emulsification, emulsifier unit is closed, opening circulating water cooling and agitating device, (revolving speed is
300r/min), when material temperature being made to be gradually decreased to 35 DEG C or so, the aerobic fermentation microbial inoculum of 1% mass, including bacillus subtilis are put into
Bacterium: saccharomyces cerevisiae: produce gastral cavity Candida: Aspergillus cooperates by the mass ratio of 1:2:1:1:0.5, puts into 0.1% and answers
Synthase preparation, including neutral proteinase: neutral lipase is cooperated by 1:1 mass ratio；Be then turned on emulsification, mixing arrangement into
The fully emulsified mixing of row 30 minutes；
D. after sterilizing emulsification, every 30min stirring gas supply 10min is set, ferments 24 hours in 30 DEG C, carries out aerobic fermentation；
E. aerobic fermentation terminates, and anaerobic fermentation microbial inoculum, including lactobacillus plantarum is added: enterococcus faecalis: lactobacillus acidophilus is pressed
The mass ratio of 1:2:1 cooperates, and is uniformly mixed, and self-controlled circulating 10min/3h is arranged, and ferments 24 hours in 30 DEG C,
Carry out anaerobism flavouring；
F. product after anaerobic fermentation is odorless, micro-perfume, the product after being processed；The product keeps in sealed storage
It carries out storing in tank stand-by.
Embodiment three: the method two of emulsification glycolysis device emulsification glycolysis processing meat packing by-product:
A. chicken carcasses thawed, cleaned, is then lifted out in investment pulverizer, opened pulverizer and carry out at pre- rubbing
Reason；
B. the material after rubbing is sent into the fermentor for being set to and rubbing motor spindle, and proper amount of clear water is added (to flood emulsification
The rack of device is advisable), open heating water bath, emulsifier unit (revolving speed 1400r/min) and agitating device (revolving speed 300r/
Min), sterilizing emulsification treatment is carried out to material, when material temperature reaches 80 DEG C or so, stop heating and insulated sterilizing 30 minutes with
On；
C. after the completion of material sterilizing emulsification, emulsifier unit is closed, opening circulating water cooling and agitating device, (revolving speed is
200r/min), when material temperature being made to be gradually decreased to 35 DEG C or so, the aerobic fermentation microbial inoculum of 1% mass, including bacillus subtilis are put into
Bacterium: saccharomyces cerevisiae: produce gastral cavity Candida: Aspergillus cooperates by the mass ratio of 1:2:1:1:0.5, puts into 0.1% and answers
Synthase preparation, including neutral proteinase: neutral lipase is cooperated by 1:1 mass ratio；Be then turned on emulsification, mixing arrangement into
The fully emulsified mixing of row 30 minutes；
D. after sterilizing emulsification, every 30min stirring gas supply 10min is set, ferments 24 hours in 35 DEG C, carries out aerobic fermentation；
E. aerobic fermentation terminates, and anaerobic fermentation microbial inoculum, including lactobacillus plantarum is added: enterococcus faecalis: lactobacillus acidophilus is pressed
The mass ratio of 1:2:1 cooperates, and is uniformly mixed, and self-controlled circulating 10min/3h is arranged, and ferments 24 hours in 35 DEG C,
Carry out anaerobism flavouring；
F. product after anaerobic fermentation is odorless, micro-perfume, the product after being processed；The product keeps in sealed storage
It carries out storing in tank stand-by.
Example IV: the method three of emulsification glycolysis device emulsification glycolysis processing meat packing by-product:
A. chicken carcasses thawed, cleaned, is then lifted out in investment pulverizer, opened pulverizer and carry out at pre- rubbing
Reason；
B. the material after rubbing is sent into the fermentor for being set to and rubbing motor spindle, and proper amount of clear water is added (to flood emulsification
The rack of device is advisable), open heating water bath, emulsifier unit (revolving speed 1400r/min) and agitating device (revolving speed 250r/
Min), sterilizing emulsification treatment is carried out to material, when material temperature reaches 80 DEG C or so, stop heating and insulated sterilizing 30 minutes with
On；
C. after the completion of material sterilizing emulsification, emulsifier unit is closed, opening circulating water cooling and agitating device, (revolving speed is
250r/min), when material temperature being made to be gradually decreased to 35 DEG C or so, the aerobic fermentation microbial inoculum of 1% mass, including bacillus subtilis are put into
Bacterium: saccharomyces cerevisiae: produce gastral cavity Candida: Aspergillus cooperates by the mass ratio of 1:2:1:1:0.5, puts into 0.1% and answers
Synthase preparation, including neutral proteinase: neutral lipase is cooperated by 1:1 mass ratio；Be then turned on emulsification, mixing arrangement into
The fully emulsified mixing of row 30 minutes；
D. after sterilizing emulsification, every 30min stirring gas supply 10min is set, ferments 24 hours in 33 DEG C, carries out aerobic fermentation；
E. aerobic fermentation terminates, and anaerobic fermentation microbial inoculum, including lactobacillus plantarum is added: enterococcus faecalis: lactobacillus acidophilus is pressed
The mass ratio of 1:2:1 cooperates, and is uniformly mixed, and self-controlled circulating 10min/3h is arranged, and ferments 24 hours in 33 DEG C,
Carry out anaerobism flavouring；
F. product after anaerobic fermentation is odorless, micro-perfume, the product after being processed；The product keeps in sealed storage
It carries out storing in tank stand-by.
Embodiment five: application of the emulsification glycolysis device in fruits and vegetables deep processing
A. fruits and vegetables are promoted in investment pulverizer, opens pulverizer and carries out pre- rubbing processing；
B. the material after rubbing is sent into the fermentor for being set to and rubbing motor spindle, and proper amount of clear water is added (to flood emulsification
The rack of device is advisable), open heating water bath, emulsifier unit (revolving speed 1400r/min) and agitating device (revolving speed 250r/
Min), sterilizing emulsification treatment is carried out to material, when material temperature reaches 80 DEG C or so, stop heating and insulated sterilizing 30 minutes with
On；
C. after the completion of material sterilizing emulsification, emulsifier unit is closed, opening circulating water cooling and agitating device, (revolving speed is
250r/min), when material temperature being made to be gradually decreased to 35 DEG C or so, the aerobic fermentation microbial inoculum of 1% mass, including bacillus subtilis are put into
Bacterium: saccharomyces cerevisiae: produce gastral cavity Candida: Aspergillus cooperates by the mass ratio of 1:2:1:1:0.5, puts into 0.1% and answers
Synthase preparation, including neutral proteinase: neutral lipase is cooperated by 1:1 mass ratio；Be then turned on emulsification, mixing arrangement into
The fully emulsified mixing of row 30 minutes；
D. after sterilizing emulsification, every 30min stirring gas supply 10min is set, ferments 24 hours in 33 DEG C, carries out aerobic fermentation；
E. aerobic fermentation terminates, and anaerobic fermentation microbial inoculum, including lactobacillus plantarum is added: enterococcus faecalis: lactobacillus acidophilus is pressed
The mass ratio of 1:2:1 cooperates, and is uniformly mixed, and self-controlled circulating 10min/3h is arranged, and ferments 24 hours in 33 DEG C,
Carry out anaerobism flavouring；
F. product after anaerobic fermentation is odorless, micro-perfume, the product after being processed；The product keeps in sealed storage
It carries out storing in tank stand-by.
Embodiment six: emulsification glycolysis device utilizes chicken preparation function ferment fertilizer of dying of illness
A. the chicken that will die of illness is promoted in investment pulverizer, is opened pulverizer and is carried out pre- rubbing processing；
B. the material after rubbing is sent into the fermentor for being set to and rubbing motor spindle, and proper amount of clear water is added (to flood emulsification
The rack of device is advisable), open heating water bath, emulsifier unit (revolving speed 1400r/min) and agitating device (revolving speed 250r/
Min), sterilizing emulsification treatment is carried out to material, when material temperature reaches 900 DEG C or so, stop heating and insulated sterilizing 30 minutes with
On；
C. after the completion of material sterilizing emulsification, emulsifier unit is closed, opening circulating water cooling and agitating device, (revolving speed is
250r/min), when material temperature being made to be gradually decreased to 35 DEG C or so, the aerobic fermentation microbial inoculum of 1% mass, including bacillus subtilis are put into
Bacterium: saccharomyces cerevisiae: produce gastral cavity Candida: Aspergillus cooperates by the mass ratio of 1:2:1:1:0.5, puts into 0.1% and answers
Synthase preparation, including neutral proteinase: neutral lipase is cooperated by 1:1 mass ratio；Be then turned on emulsification, mixing arrangement into
The fully emulsified mixing of row 30 minutes；
D. after sterilizing emulsification, every 30min stirring gas supply 10min is set, ferments 24 hours in 33 DEG C, carries out aerobic fermentation；
E. aerobic fermentation terminates, and anaerobic fermentation microbial inoculum, including lactobacillus plantarum is added: enterococcus faecalis: lactobacillus acidophilus is pressed
The mass ratio of 1:2:1 cooperates, and is uniformly mixed, and self-controlled circulating 10min/3h is arranged, and ferments 24 hours in 33 DEG C,
Carry out anaerobic fermentation；
F. product after anaerobic fermentation is odorless, micro-perfume, the product after being processed；The product keeps in sealed storage
It carries out storing for use in tank, can be used for preparing functional biological bacterial manure.
It should be understood that these examples are only for illustrating the present invention and are not intended to limit the scope of the present invention.In addition, it should also be understood that,
After reading the content taught by the present invention, those skilled in the art can make various modifications or changes to the present invention, these
Equivalent form is also fallen within the scope of the appended claims of the present application.
Claims (10)
1. a kind of emulsification glycolysis device, it is characterised in that: including emulsification fermentor and the pulverizer being disposed thereon, the rubbing
The discharge port of machine is communicated to the feed inlet of emulsification fermentor；
Emulsifying fermentor includes tank body, and the top of the tank body is equipped with feed inlet, and bottom is equipped with discharge port；The tank body peripheral wall by
Double-layer stainless steel forms, and is welded with circulating coil on internal layer inner wall；The tank interior is additionally provided with agitating device and emulsification dress
It sets, the agitating device includes the stirring motor for being provided with tank deck, and the stirring motor lower part is connected with speed reducer, the deceleration
Machine lower part is connected with agitating shaft, and the agitating shaft top is equipped with defoaming rake, is provided with 5~8 at the shaft bottom port
Stirring blade；Air inlet and air outlet are additionally provided on the tank body.
2. emulsification glycolysis device as described in claim 1, it is characterised in that: the circulating coil is connected to external heating water
Case is additionally provided with more than one temperature sensor in the tank body.
3. emulsification glycolysis device as described in claim 1, it is characterised in that: the emulsifier unit is set to tank base, packet
The emulsification motor being set on the outside of tank base is included, the emulsification motor top is equipped with transmission shaft, and the transmission shaft passes through tank body
It enters and is set to inside the frame housing of tank base；The bottom of the frame of the emulsifier unit is closed disk, the circle
Disk top is fixedly connected with the shell of circular hollow upwards, and the lower part of the housing is provided with more than one hollow out mouth, the shell
It is upper parallel to be provided with several grooves；Agitating paddle is provided on the transmission shaft of enclosure interior.
4. emulsification glycolysis device as claimed in claim 3, it is characterised in that: several grooves of the upper part of the housing are oblique flat
Row setting.
5. emulsification glycolysis device as described in claim 1, it is characterised in that: defoaming rake lower part is provided with more than one
Defoam tooth.
6. a kind of method using emulsification glycolysis device emulsification glycolysis described in claim 1, it is characterised in that including following step
It is rapid:
A. material is cleaned, puts into pulverizer and carries out pre- rubbing processing；
B. the material after rubbing is sent into the fermentor for being set to and rubbing motor spindle, and proper amount of clear water is added, and opens heating water bath, cream
Makeup is set and agitating device, carries out sterilizing emulsification treatment to material, when material temperature reaches 80 DEG C or so, stops heating and keeping the temperature going out
Bacterium 30 minutes or more；
C. after the completion of material sterilizing emulsification, emulsifier unit is closed, circulating water cooling and agitating device is opened, is gradually decreased to material temperature
At 35 DEG C or so, the aerobic fermentation microbial inoculum of 1% mass ratio is put into, while putting into 0.1% complex enzyme formulation；It is then turned on cream
Change, mixing arrangement carries out fully emulsified mixing 30 minutes；
D. after sterilizing emulsification, every 30min stirring gas supply 10min is set, ferments 24 hours in 30~35 DEG C, carries out aerobic fermentation；
E. aerobic fermentation terminates, and anaerobic fermentation microbial inoculum is added, and be uniformly mixed, and self-controlled circulating 10min/3h is arranged, in 30
~35 DEG C ferment 24 hours, carry out anaerobism flavouring；
F. the product after being processed after anaerobic fermentation.
7. the method for emulsification glycolysis as claimed in claim 6, it is characterised in that: the revolving speed of the emulsification in the step b is
1400rpm；The revolving speed of stirring is 200rpm to 300rpm；The revolving speed stirred in the step d is 200rpm to 300rpm；Oxygen supply
Amount is 1.6M3/min。
8. the method for emulsification glycolysis as claimed in claim 6, it is characterised in that: the revolving speed stirred in the step c is
200rpm to 300rpm；The aerobic fermentation microbial inoculum includes bacillus subtilis: saccharomyces cerevisiae: producing gastral cavity Candida: Aspergillus
Cooperate by the mass ratio of 1:2:1:1:0.5, wherein bacillus subtilis, saccharomyces cerevisiae and the viable bacteria for producing gastral cavity Candida
Every gram of number is respectively 1.0~5.0 × 108It is a；The complex enzyme formulation includes neutral proteinase and neutral lipase by 1:1 mass
Than cooperating.
9. the method for emulsification glycolysis as claimed in claim 6, it is characterised in that: the revolving speed of the stirring in the step e is
200rpm to 300rpm；The anaerobic fermentation microbial inoculum includes lactobacillus plantarum: enterococcus faecalis: lactobacillus acidophilus by 1:2:1 matter
Amount ratio cooperates, wherein lactobacillus plantarum: enterococcus faecalis: every gram of viable count of lactobacillus acidophilus respectively 1.0~5.0 ×
108It is a.
10. the application of any emulsification glycolysis device of claim 1 to 5, it is characterised in that: the emulsification glycolysis device can
Applied to meat product deep processing, deep processing of farm products, microbiological feed production and the production of agricultural microorganism bacterial manure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910661423.0A CN110499244A (en) | 2019-07-22 | 2019-07-22 | A kind of emulsification glycolysis device and emulsification glycolysis method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910661423.0A CN110499244A (en) | 2019-07-22 | 2019-07-22 | A kind of emulsification glycolysis device and emulsification glycolysis method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN110499244A true CN110499244A (en) | 2019-11-26 |
Family
ID=68586647
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910661423.0A Pending CN110499244A (en) | 2019-07-22 | 2019-07-22 | A kind of emulsification glycolysis device and emulsification glycolysis method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110499244A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2021184928A1 (en) * | 2020-03-19 | 2021-09-23 | 李茂正 | Improved structure of stirring tank equipment |
| CN114516772A (en) * | 2021-08-30 | 2022-05-20 | 鹤壁市禾盛生物科技有限公司 | Rapid fermentation preparation method of high-nitrogen organic liquid fertilizer |
| CN116970486A (en) * | 2023-09-25 | 2023-10-31 | 山东兴合盛生物科技有限公司 | Enzymolysis device is used in collagen peptide production |
Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TW509103U (en) * | 2001-12-27 | 2002-11-01 | Minoga Indusetial Co Ltd | Improved structure for emulsifying head of emulsifying and stirring machine |
| CN101720853A (en) * | 2009-10-19 | 2010-06-09 | 李军训 | Technology for fermenting and decomposing protein feed with protease in two steps by using probiotics |
| CN203944340U (en) * | 2014-06-09 | 2014-11-19 | 柳州市豪杰特化工机械有限责任公司 | A kind of emulsifying head |
| CN204841550U (en) * | 2015-06-24 | 2015-12-09 | 广州市著力化工设备有限公司 | Homogenous emulsification head |
| CN105360625A (en) * | 2015-09-24 | 2016-03-02 | 季维峰 | Solid phase double dynamic enzymolysis and fermentation process of plant-derived organic matter |
| JP2018008247A (en) * | 2016-07-15 | 2018-01-18 | Ｋｙｂ株式会社 | Agitation device and agitation method |
| CN207271085U (en) * | 2017-09-09 | 2018-04-27 | 上海禾雅化妆品有限公司 | Emulsifying homogeneous machine |
| CN208454940U (en) * | 2018-05-26 | 2019-02-01 | 广州市宝桃食品有限公司 | A kind of fermentation emulsification unit equipment |
| CN109402013A (en) * | 2018-11-20 | 2019-03-01 | 江南大学 | A kind of high temperature resistant bacillus subtilis of yielding lipase and its application in compost |
| CN208839423U (en) * | 2018-08-15 | 2019-05-10 | 河北益存生物科技有限公司 | A kind of emulsion tank |
-
2019
- 2019-07-22 CN CN201910661423.0A patent/CN110499244A/en active Pending
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TW509103U (en) * | 2001-12-27 | 2002-11-01 | Minoga Indusetial Co Ltd | Improved structure for emulsifying head of emulsifying and stirring machine |
| CN101720853A (en) * | 2009-10-19 | 2010-06-09 | 李军训 | Technology for fermenting and decomposing protein feed with protease in two steps by using probiotics |
| CN203944340U (en) * | 2014-06-09 | 2014-11-19 | 柳州市豪杰特化工机械有限责任公司 | A kind of emulsifying head |
| CN204841550U (en) * | 2015-06-24 | 2015-12-09 | 广州市著力化工设备有限公司 | Homogenous emulsification head |
| CN105360625A (en) * | 2015-09-24 | 2016-03-02 | 季维峰 | Solid phase double dynamic enzymolysis and fermentation process of plant-derived organic matter |
| JP2018008247A (en) * | 2016-07-15 | 2018-01-18 | Ｋｙｂ株式会社 | Agitation device and agitation method |
| CN207271085U (en) * | 2017-09-09 | 2018-04-27 | 上海禾雅化妆品有限公司 | Emulsifying homogeneous machine |
| CN208454940U (en) * | 2018-05-26 | 2019-02-01 | 广州市宝桃食品有限公司 | A kind of fermentation emulsification unit equipment |
| CN208839423U (en) * | 2018-08-15 | 2019-05-10 | 河北益存生物科技有限公司 | A kind of emulsion tank |
| CN109402013A (en) * | 2018-11-20 | 2019-03-01 | 江南大学 | A kind of high temperature resistant bacillus subtilis of yielding lipase and its application in compost |
Non-Patent Citations (1)
| Title |
|---|
| 方祖成，李冬生，汪超: "《食品工厂机械装备》", 30 June 2017 * |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2021184928A1 (en) * | 2020-03-19 | 2021-09-23 | 李茂正 | Improved structure of stirring tank equipment |
| CN113491977A (en) * | 2020-03-19 | 2021-10-12 | 李茂正 | Improved structure of stirring tank equipment |
| CN114516772A (en) * | 2021-08-30 | 2022-05-20 | 鹤壁市禾盛生物科技有限公司 | Rapid fermentation preparation method of high-nitrogen organic liquid fertilizer |
| CN116970486A (en) * | 2023-09-25 | 2023-10-31 | 山东兴合盛生物科技有限公司 | Enzymolysis device is used in collagen peptide production |
| CN116970486B (en) * | 2023-09-25 | 2023-12-22 | 山东兴合盛生物科技有限公司 | Enzymolysis device is used in collagen peptide production |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100546491C (en) | Animal fermented concentrated feed and mixed feed and preparation method thereof and equipment | |
| CN101760431B (en) | A kind of compound microbial culture starter and application thereof | |
| CN101297677B (en) | Technique for detoxicating rapeseed dregs and modifying rapeseed proteins by synchronous bacterium mixing and fermenting method | |
| CN101531985B (en) | High-efficiency ferment for fermenting bean pulp and bean pulp fermentation technology using the ferment | |
| CN110499244A (en) | A kind of emulsification glycolysis device and emulsification glycolysis method | |
| CN106365788A (en) | Harmless microorganism treatment method for cadavers of livestock and poultry | |
| CN103444985B (en) | Feed additive and manufacturing method and application thereof | |
| CN102660436A (en) | Oyster yellow wine | |
| CN107047932A (en) | A kind of utilization breeding waste produces the production technology of microbiological culture media | |
| CN108975959A (en) | A kind of organic food waste integral biological fermentation fertilizer production apparatus | |
| CN107319196A (en) | A kind of microorganism formulation for improving fresh-water fishes function of intestinal canal and application thereof | |
| CN105360625A (en) | Solid phase double dynamic enzymolysis and fermentation process of plant-derived organic matter | |
| CN102311929A (en) | Method for largely and rapidly reproducing lactic acid bacteria | |
| CN101897659A (en) | Method for preparing enzyme warm bath material by probiotic solid fermentation technology | |
| CN103070287B (en) | Lactobacillus paracasei fermented feed and preparation method thereof, fermenting equipment and application of lactobacillus paracasei fermented feed | |
| CN104649763B (en) | A kind of method of the intensive vaccary excreta of Anaerobic Treatment | |
| CN101653189B (en) | Natural plant small molecular group substance concentrate and production method thereof | |
| CN109170151A (en) | The preparation method of fermentative feedstuff of microbe | |
| CN209121194U (en) | A kind of microbial fermentation detoxification device of dregs of rapeseed cake | |
| CN106929455A (en) | A kind of zymotechnique that composite thallus protein feed is produced using agricultural and sideline poor slag | |
| CN104031971A (en) | Producing method of N-carbamylglutamate by free cell fermentation method, and applications of metabolites of the N-carbamylglutamate | |
| CN109221611A (en) | A kind of method that the fermentation of cattle and sheep gastric content prepares feed | |
| CN103519028B (en) | A kind of broiler breeding feed and method for breeding thereof | |
| CN103202412A (en) | Biological preservation processing and producing method for rice bran | |
| CN208038444U (en) | A kind of degradation of feather and installation for fermenting |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20191126 |