CN209219218U - A kind of digested tankage production equipment - Google Patents
A kind of digested tankage production equipment Download PDFInfo
- Publication number
- CN209219218U CN209219218U CN201821892069.XU CN201821892069U CN209219218U CN 209219218 U CN209219218 U CN 209219218U CN 201821892069 U CN201821892069 U CN 201821892069U CN 209219218 U CN209219218 U CN 209219218U
- Authority
- CN
- China
- Prior art keywords
- water
- digested tankage
- screw conveyor
- production equipment
- filter
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Landscapes
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Abstract
The utility model discloses a kind of digested tankage production equipments, belong to digested tankage production technical field.Its technical solution are as follows: including jetting machine, ice breaker, change rouge tank and the double spiral squeezer being successively linked in sequence by screw conveyor；One discharge port of the double spiral squeezer is connected with drying chamber by screw conveyor, another discharge port is connected with water-oil separating centrifuge by screw conveyor；The drying chamber is connected with cooler by screw conveyor；The cooler is connected with storage bin by screw conveyor；The cooler is connected with bag filter by pipeline；The bag filter is equipped with air-introduced machine；The oil outlet of the water-oil separating centrifuge is connected with oil storage tank by screw conveyor.The utility model is fully extracted the high protein in raw material, realizes the recycling of waste water, avoids the loss of nutritional ingredient, has saved cost.And working environment is improved, the pollution to atmosphere is greatly reduced, environmental protection is conducive to.
Description
Technical field
The utility model relates to digested tankage production technical fields, more particularly to a kind of digested tankage production equipment.
Background technique
Digested tankage production be will raise, leftover bits and pieces that fowl and other animal products generate in process is (mainly including animal
Internal organ, meat mincing, fat and inedibility animal tissues' organ such as carcass) be processed into digested tankage feed, using wherein containing abundant
Protein and energy, for raising animal good calcium, phosphorus source are provided, solve animal protein in existing feed, fat not
The problem of foot.
But existing digested tankage production equipment has the following problems:
1. existing equipment is when producing digested tankage, do not extract the high protein in animal tissue's organ sufficiently, cause nutrition at
The loss divided.
2. the direct emissions such as the waste water generated in production process, exhaust gas, dust cause environmental pollution, the work of staff
Make that environment is poor, seriously affects the health of staff.
Utility model content
The utility model provides a kind of digested tankage production equipment, the bone collagen being further extracted in production waste water,
The recycling for realizing waste water avoids the loss of nutritional ingredient, has saved cost.High degree of automation substantially increases
Production efficiency, while atmosphere pollution is decreased, working environment is improved, environmental protection is conducive to.
The technical solution of the utility model are as follows:
A kind of digested tankage production equipment, including jetting machine, the ice breaker, change being successively linked in sequence by screw conveyor
Rouge tank and double spiral squeezer；One discharge port of the double spiral squeezer is connected with drying chamber by screw conveyor, separately
One discharge port is connected with water-oil separating centrifuge by screw conveyor；The drying chamber is connected with cold by screw conveyor
But machine；The cooler is connected with storage bin by screw conveyor；The cooler is connected with bag filter by pipeline；
The bag filter is equipped with air-introduced machine；The oil outlet of the water-oil separating centrifuge is connected with oil storage by screw conveyor
Tank；The water outlet of the water-oil separating centrifuge is connect by water-supply-pipe with wastewater recycling system, and Sewage treatment utilizes system
System treated water is connect by water-supply-pipe with drying chamber；Describedization rouge tank, drying chamber and storage bin pass through pipeline respectively and remove
Smelly equipment connection.
Preferably, the wastewater recycling system include the enzymatic hydrolysis stirred autoclave being successively linked in sequence by pipeline,
First filter, centrifugal separator, the second filter and dual-effect concentrator；The waterwater entrance of the enzymatic hydrolysis stirred autoclave passes through
Water-supply-pipe is connected with the water outlet of water-oil separating centrifuge；The bone collagen outlet of the dual-effect concentrator is connected by pipeline
There is drying machine；The water outlet of dual-effect concentrator is connect by water-supply-pipe with drying chamber.
Preferably, vacuum jacket is equipped with outside the enzymatic hydrolysis stirred autoclave, the vacuum jacket is equipped with vacuum orifice.
Preferably, the first filter is equipped with ultrafiltration membrane.
Preferably, the ultrafiltration membrane aperture is 0.005 micron.
Preferably, second filter is equipped with nanofiltration membrane.
Preferably, the nanofiltration membrane aperture is 1.5 nanometers.
Preferably, the enzymatic hydrolysis stirred autoclave bottom is taper.
Preferably, the enzymatic hydrolysis stirred autoclave, first filter, centrifugal separator, the second filter, dual-effect concentrator
It is stainless steel material with drying machine.
The utility model has the following beneficial effects:
1. in the digested tankage production equipment of the utility model, waste water being added between water-oil separating centrifuge and drying chamber and is returned
The system of utilizing is received, wastewater recycling system is first passed through and extracts bone collagen in water, bone collagen powder is made, then
Remaining water is delivered in drying chamber, the baking process of digested tankage is participated in, by protein salvage remaining in water in digested tankage, is avoided
The loss of albumen.And it is fully extracted the high protein in raw material, the recycling of waste water is realized, nutritional ingredient is avoided
It is lost, has saved cost.High degree of automation substantially increases production efficiency.
2. the digested tankage production equipment of the utility model is stored in autoclaving process, digested tankage baking process and digested tankage
The exhaust gas generated in the process is concentrated through after deodorizing device carries out deodorizing process and discharges again, and, it is produced in digested tankage cooling procedure
Raw dust is dusted processing by bag filter, improves working environment, greatly reduces the pollution to atmosphere, is conducive to
Environmental protection.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model.
Fig. 2 is the structural schematic diagram of the wastewater recycling system of the utility model.
Description of symbols: 1- screw conveyor, 2- jetting machine, 3- ice breaker, 4-ization rouge tank, the squeezing of 5- double helix
Machine, 6- drying chamber, 7- water-oil separating centrifuge, 8- cooler, 9- storage bin, 10- bag filter, 11- air-introduced machine, 12- storage
Oil tank, 13- water-supply-pipe, 14- deodorizing device, 15- wastewater recycling system, 16- enzymatic hydrolysis stirred autoclave, 17- first are filtered
Device, 18- centrifugal separator, the second filter of 19-, 20- dual-effect concentrator, 21- drying machine, 22- vacuum jacket, 23- are vacuumized
Mouthful.
Specific embodiment
The technology of the utility model is described in detail in the utility model in order to better understand with specific embodiment below
Scheme, but the utility model is not limited thereto.
Embodiment 1
A kind of digested tankage production equipment is present embodiments provided, including the high pressure being successively linked in sequence by screw conveyor 1
Cleaning machine 2, changes rouge tank 4 and double spiral squeezer 5 at ice breaker 3；One discharge port of the double spiral squeezer 5 passes through spiral
Conveyer 1 is connected with drying chamber 6, another discharge port is connected with water-oil separating centrifuge 7 by screw conveyor 1；It is described dry
Dry tank 6 is connected with cooler 8 by screw conveyor 1；The cooler 8 is connected with storage bin 9 by screw conveyor 1；Institute
It states cooler 8 and bag filter 10 is connected with by pipeline；The bag filter 10 is equipped with air-introduced machine 11；The grease point
The oil outlet of luxuriant scheming 7 is connected with oil storage tank 12 by screw conveyor 1；The water outlet of the water-oil separating centrifuge 7 is logical
It crosses water-supply-pipe 13 to connect with wastewater recycling system 15, treated the water of wastewater recycling system 15 passes through water-supply-pipe and dry
Dry tank 6 connects；Describedization rouge tank 4, drying chamber 6 and storage bin 9 are connect by pipeline with deodorizing device 14 respectively.
Wherein, the wastewater recycling system includes that the enzymatic hydrolysis stirring for the stainless steel being successively linked in sequence by pipeline is anti-
Kettle 16, first filter 17, centrifugal separator 18, the second filter 19 and dual-effect concentrator 20 are answered, stirred autoclave 16 is digested
Bottom is taper；The waterwater entrance of the enzymatic hydrolysis stirred autoclave 16 passes through the water outlet of water-supply-pipe and water-oil separating centrifuge 7
It is connected；The bone collagen of the dual-effect concentrator 20, which is exported, is connected with drying machine 21 by pipeline；Dual-effect concentrator 20 goes out
The mouth of a river is connect by water-supply-pipe with drying chamber 6.
The first filter 17 is equipped with the ultrafiltration membrane that aperture is 0.005 micron；Second filter 19 is equipped with aperture
For 1.5 nanometers of nanofiltration membrane.The ultrafiltration membrane and nanofiltration membrane of special pore size distribution size are for bone collagen powder product produced
Depending on the requirement of purity.
When producing digested tankage using the digested tankage production equipment of the present embodiment, production technology is as follows:
S1: after animal tissue's organ is cleaned up in jetting machine 2, the ice-breaking in ice breaker 3；
S2: the animal tissue organ 0.5-2h after changing the 4 high temperature boiling ice-breaking of rouge tank, thermophilic digestion temperature are set as 130-
150 DEG C, preferably 140 DEG C can reach farthest high-temperature sterilization effect under the premise of save the cost under the conditions of this temperature
Fruit；The exhaust gas generated in the process discharges after carrying out deodorizing process by deodorizing device 14；
S3: animal tissue's organ after thermophilic digestion is carried out to three sections of squeezing degreasings, one section of pressure in double spiral squeezer 5
Squeezing power is 2MPa, and two sections of squeeze pressures are 4MPa, and three sections of squeeze pressures are 5MPa；
S4: animal tissue's organ output digested tankage and oil water mixture after squeezing degreasing, wherein by digested tankage in drying chamber 6
Drying, drying temperature are 140-150 DEG C；The exhaust gas generated in drying course discharges after 14 deodorizing process of deodorizing device, will be oily
Aqueous mixtures carry out water-oil separating in water-oil separating centrifuge 7；
S5: it is cooled by the digested tankage after 8 pairs of cooler drying, by bag filter 10 to being generated in cooling procedure
Dust dedusting, be delivered in storage bin 9 and store after digested tankage after cooling pack, the exhaust gas generated during storage is set through deodorization
It is discharged after standby 14 progress deodorizing process；
S6: the oil after water-oil separating send to oil storage tank 12 and stores, and water is then sent into wastewater recycling system 15, extracts it
In bone collagen after, remaining water is delivered to again in drying chamber 6.
Wherein, in S6, as shown in Fig. 2, the method for extracting bone collagen in water is to introduce the water into Sewage treatment using system
System 15 enzymatic hydrolysis stirred autoclave 16 in, 80 DEG C or so at a temperature of it is digested, digest bone collagen, water and
Grease, wherein bone collagen is soluble in water.Waste water after enzymatic hydrolysis, which enters, carries out ultrafiltration in first filter 17, get rid of it
In the solid impurities such as bone slag.Filtrate is centrifuged in subsequent centrifugal separator 18, obtains separating liquid, grease and remnants
Bone slag improves protein content in the bone collagen powder of subsequent production to realize the removing of grease in waste water.Separating liquid is defeated
It send and carries out secondary nanofiltration into the second filter 19, further get rid of the bone slag being entrained in separating liquid.By to waste water into
Row filters twice, and the filtering accuracy of secondary filter is higher than primary filtering, can be clean by the removal of the impurity such as bone slag therein, protects
The quality of bone collagen powder product is demonstrate,proved.Filtrate after secondary nanofiltration is the bone collagen for being dissolved in water, is then gone through double
It is concentrated in effect inspissator 20.In concentration process, the moisture in filtrate is finally delivered to drying chamber through pervaporation and condensation
In 6, the baking process of digested tankage is participated in, by protein salvage remaining in water in digested tankage, avoids the loss of albumen.And in concentrate
The concentration of bone collagen is gradually increased with the evaporation of moisture, when concentration reaches certain standard, bone collagen concentrate
Discharge is exported by the bone collagen of dual-effect concentrator 20, enters in drying machine 21 and is dried, wherein drying machine 21 can make
With drying equipments such as vacuum freeze driers.Bone collagen concentrate after drying to get arrive bone collagen powder product.
Further, in the present embodiment, vacuum jacket 22, the vacuum are equipped with outside the enzymatic hydrolysis stirred autoclave 16
Collet 22 is equipped with vacuum orifice 23.
Vacuum jacket 22 is vacuumized by vacuum orifice 23, so that formation one is heat-insulated outside enzymatic hydrolysis stirred autoclave 16
Layer reduces the heat exchange between inside and outside enzymatic hydrolysis stirred autoclave 16, keeps the stability of temperature in enzymatic hydrolysis stirred autoclave 16,
To ensure that the high activity of enzyme in enzymatic hydrolysis stirred autoclave 16, the efficiency of enzyme digestion reaction and the extraction of bone collagen are improved
Rate.
Digested tankage is produced using the digested tankage production equipment of the present embodiment, water-oil separating is extracted by wastewater recycling system 15
Bone collagen in waste water afterwards, to produce bone collagen powder, with directly by discharge of wastewater compared with, the present embodiment sufficiently returns
The high protein for having received raw material avoids the loss of nutritional ingredient, has saved cost.And it is extracted the return of the water after bone collagen
To drying chamber 6, the baking process of digested tankage is participated in, by protein salvage remaining in water in digested tankage, is taken full advantage of in water
Albumen avoids the loss of nutrition.
Meanwhile in process of production, the conveying of material greatly reduces work by screw conveyor 1, high degree of automation
The labor intensity of people, improves production efficiency.It is produced to during the storage of autoclaving process, digested tankage baking process and digested tankage
Raw exhaust gas is concentrated through after deodorizing device 14 carries out deodorizing process and discharges again, and, the powder generated in digested tankage cooling procedure
Dirt is dusted processing by bag filter 10, improves working environment, greatly reduces the pollution to atmosphere, is conducive to ring
It protects.
Embodiment 2
It is in place of the present embodiment and the difference of embodiment 1: S3: by animal tissue's organ after thermophilic digestion in double helix
Three sections of squeezing degreasings are carried out in squeezer 5, one section of squeeze pressure is 0.5MPa, and two sections of squeeze pressures are 2.5MPa, three sections of squeezings
Pressure is 4.5MPa.
Embodiment 3
It is in place of the present embodiment and the difference of embodiment 1: S3: by animal tissue's organ after thermophilic digestion in double helix
Three sections of squeezing degreasings are carried out in squeezer 5, one section of squeeze pressure is 1MPa, and two sections of squeeze pressures are 3MPa, three sections of squeeze pressures
For 6MPa.
Digested tankage water content after single pressing is 21%-29%, and the digested tankage after three sections of squeezings of embodiment 1-3 contains
Water is 9-16%, it can be seen that, to after thermophilic digestion animal tissue's organ carry out three sections of squeezing degreasings, and squeeze pressure by
Duan Zeng great, so that animal tissue's organ degreasing is more thorough, the digested tankage water content of output also can be lower after degreasing, facilitates subsequent baking
Dry process, improves production efficiency.
Specific embodiment of the present utility model is described in detail in conjunction with attached drawing above, but the utility model is not
It is limited to the detail of above embodiment, those skilled in the art are in the technical solution of the utility model range
Interior made modification, addition or replacement, also belong to the protection scope of the utility model.
It is further to note that in the case of no contradiction, between each different embodiment of the utility model
It can also in any combination, as long as it, without prejudice to the thought of the utility model, equally should be considered as disclosed in the utility model
Content.
Claims (9)
1. a kind of digested tankage production equipment, it is characterised in that:
Including jetting machine, ice breaker, change rouge tank and the double spiral squeezer being successively linked in sequence by screw conveyor；
One discharge port of the double spiral squeezer is connected with drying chamber by screw conveyor, another discharge port passes through spiral shell
Rotation conveyer is connected with water-oil separating centrifuge；
The drying chamber is connected with cooler by screw conveyor；
The cooler is connected with storage bin by screw conveyor；
The cooler is connected with bag filter by pipeline；
The bag filter is equipped with air-introduced machine；
The oil outlet of the water-oil separating centrifuge is connected with oil storage tank by screw conveyor；
The water outlet of the water-oil separating centrifuge is connect by water-supply-pipe with wastewater recycling system, and Sewage treatment utilizes system
System treated water is connect by water-supply-pipe with drying chamber；
Describedization rouge tank, drying chamber and storage bin pass through pipeline respectively and connect with deodorizing device.
2. digested tankage production equipment as described in claim 1, it is characterised in that: the wastewater recycling system includes passing through pipe
Enzymatic hydrolysis stirred autoclave, first filter, centrifugal separator, the second filter and the dual-effect concentrator that road is successively linked in sequence；
The waterwater entrance of the enzymatic hydrolysis stirred autoclave is connected by water-supply-pipe with the water outlet of water-oil separating centrifuge；The economic benefits and social benefits are dense
The bone collagen of contracting device, which is exported, is connected with drying machine by pipeline；The water outlet of dual-effect concentrator passes through water-supply-pipe and drying chamber
Connection.
3. digested tankage production equipment as claimed in claim 2, it is characterised in that: be equipped with vacuum outside the enzymatic hydrolysis stirred autoclave
Collet, the vacuum jacket are equipped with vacuum orifice.
4. digested tankage production equipment as claimed in claim 2, it is characterised in that: the first filter is equipped with ultrafiltration membrane.
5. digested tankage production equipment as claimed in claim 4, it is characterised in that: the ultrafiltration membrane aperture is 0.005 micron.
6. digested tankage production equipment as claimed in claim 2, it is characterised in that: second filter is equipped with nanofiltration membrane.
7. digested tankage production equipment as claimed in claim 6, it is characterised in that: the nanofiltration membrane aperture is 1.5 nanometers.
8. digested tankage production equipment as claimed in claim 2, it is characterised in that: the enzymatic hydrolysis stirred autoclave bottom is taper.
9. digested tankage production equipment as claimed in claim 2, it is characterised in that: the enzymatic hydrolysis stirred autoclave, first filter,
Centrifugal separator, the second filter, dual-effect concentrator and drying machine are stainless steel material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821892069.XU CN209219218U (en) | 2018-11-16 | 2018-11-16 | A kind of digested tankage production equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821892069.XU CN209219218U (en) | 2018-11-16 | 2018-11-16 | A kind of digested tankage production equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209219218U true CN209219218U (en) | 2019-08-09 |
Family
ID=67503274
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821892069.XU Active CN209219218U (en) | 2018-11-16 | 2018-11-16 | A kind of digested tankage production equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209219218U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109170987A (en) * | 2018-11-16 | 2019-01-11 | 无棣县兴亚生物科技有限公司 | A kind of digested tankage production equipment and process |
-
2018
- 2018-11-16 CN CN201821892069.XU patent/CN209219218U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109170987A (en) * | 2018-11-16 | 2019-01-11 | 无棣县兴亚生物科技有限公司 | A kind of digested tankage production equipment and process |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101532044B (en) | A preparation method of sea cucumber collagen small peptide freeze-dried powder extracted from sea cucumber boiling liquid | |
| CN102295997B (en) | Processing method and system of kitchen waste grease | |
| CN101744090B (en) | Method for preparing small molecular peptides of soft-shelled turtle | |
| CN102793053A (en) | Technology for producing high-protein content and low-ash content plasma protein powder | |
| CN104336297B (en) | A kind of method for extracting the organic matter such as collagen in chicken bone | |
| CN108741078A (en) | The processing method for preparing the method and linseed of flaxseed gum, flax lignan, flax dietary fiber and flax protein powder | |
| CN209219218U (en) | A kind of digested tankage production equipment | |
| CN109170987A (en) | A kind of digested tankage production equipment and process | |
| CN108623714A (en) | A kind of environmental type natural rubber and preparation method thereof | |
| CN107955084B (en) | Reaction tank deslagging and separating system special for extracting chlorella polysaccharide | |
| CN114075478A (en) | Energy-saving and environment-friendly animal fat refining device and process | |
| CN115958051B (en) | Cooperative treatment system and treatment method for food wastes and kitchen wastes | |
| CN203768325U (en) | Grease production line | |
| JP2007166989A (en) | Method for treating bony part of fish | |
| CN102161652A (en) | Method for rapidly extracting anthocyanin from purple sweet potato through crushing method | |
| CN201952420U (en) | Sugar extracting system of grain emulsion | |
| CN113201522B (en) | Protease refining and drying method | |
| CN109161445A (en) | A kind of kitchen trench oil treatment system | |
| CN106071037B (en) | A kind of fish-bone peptide pre-treatment deslagging, degreasing process | |
| CN209226960U (en) | The system of bone collagen is extracted in a kind of waste water | |
| CN2910940Y (en) | Production line for extraction of shrimp head peptide protein and chitin | |
| CN112694949B (en) | Comprehensive pretreatment process for food waste and kitchen waste oil | |
| CN214458075U (en) | Device for extracting active peptide from marine fresh fish | |
| CN111760885A (en) | Novel kitchen waste treatment process flow | |
| CN110882559A (en) | High-efficient extraction element of kitchen garbage grease |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |