CN107637821A - The manufacture craft and system of a kind of concentrated bone soup - Google Patents
The manufacture craft and system of a kind of concentrated bone soup Download PDFInfo
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- CN107637821A CN107637821A CN201711058526.5A CN201711058526A CN107637821A CN 107637821 A CN107637821 A CN 107637821A CN 201711058526 A CN201711058526 A CN 201711058526A CN 107637821 A CN107637821 A CN 107637821A
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- Prior art keywords
- bone soup
- concentrated
- high pressure
- pressure resistant
- concentration
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- 210000000988 bone and bone Anatomy 0.000 title claims abstract description 63
- 235000014347 soups Nutrition 0.000 title claims abstract description 59
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 22
- 238000001728 nano-filtration Methods 0.000 claims abstract description 61
- 239000012528 membrane Substances 0.000 claims abstract description 57
- 239000012141 concentrate Substances 0.000 claims abstract description 41
- 238000005119 centrifugation Methods 0.000 claims abstract description 14
- 238000001914 filtration Methods 0.000 claims abstract description 11
- 230000000694 effects Effects 0.000 claims abstract description 9
- 239000004519 grease Substances 0.000 claims abstract description 7
- 238000000926 separation method Methods 0.000 claims abstract description 6
- 238000000034 method Methods 0.000 claims description 20
- 239000007788 liquid Substances 0.000 claims description 15
- 239000000385 dialysis solution Substances 0.000 claims description 7
- 239000000243 solution Substances 0.000 claims description 7
- 238000005096 rolling process Methods 0.000 claims description 3
- 238000000502 dialysis Methods 0.000 claims 1
- 238000005265 energy consumption Methods 0.000 abstract description 5
- 238000005516 engineering process Methods 0.000 description 3
- 235000013305 food Nutrition 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 244000144972 livestock Species 0.000 description 2
- 235000013372 meat Nutrition 0.000 description 2
- 235000016709 nutrition Nutrition 0.000 description 2
- 230000035764 nutrition Effects 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 229920002567 Chondroitin Polymers 0.000 description 1
- 241001494479 Pecora Species 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical group [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 125000001931 aliphatic group Chemical group 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- DLGJWSVWTWEWBJ-HGGSSLSASA-N chondroitin Chemical compound CC(O)=N[C@@H]1[C@H](O)O[C@H](CO)[C@H](O)[C@@H]1OC1[C@H](O)[C@H](O)C=C(C(O)=O)O1 DLGJWSVWTWEWBJ-HGGSSLSASA-N 0.000 description 1
- 239000012459 cleaning agent Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000000050 nutritive effect Effects 0.000 description 1
- 150000003904 phospholipids Chemical class 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000009738 saturating Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Landscapes
- Coloring Foods And Improving Nutritive Qualities (AREA)
- Medicines Containing Material From Animals Or Micro-Organisms (AREA)
Abstract
The invention discloses a kind of manufacture craft of concentrated bone soup, it is characterised in that comprises the steps：Step 1 centrifugal filtration：Bone soup extract solution is filtered into obtain bone soup centrifugate after centrifugation grease separation；Step 2 nanofiltration concentrates：By bone soup centrifugate after cartridge filter filters, 10 40bar are pressurized to through booster pump, the concentration of bone soup is concentrated into 20 30% using the NF membrane of the dalton of molecular cut off 50 200, obtains nanofiltration concentrate；Step 3 is concentrated in vacuo：Nanofiltration concentrate continues concentration into reduced vacuum double effect evaporator and the concentration of bone soup is concentrated into 40% 60%, obtains concentrated bone soup.Present invention additionally comprises a kind of manufacturing system of concentrated bone soup.The manufacture craft and system of concentrated bone soup of the present invention, the energy consumption of the making of concentrated bone soup can be significantly reduced, Business Economic Benefit and social benefit are clearly.
Description
Technical field
The present invention relates to concentrated bone soup field, the manufacture craft and system of more particularly to a kind of concentrated bone soup.
Background technology
Live stock and fowl bone is a kind of very high meat by- product of nutritive value, and it contains nutrition necessary to a variety of human bodies
Composition, such as protein, aliphatic acid, Phospholipids, phosphorus unit chondroitin, ossein, multivitamin.China is foster in the world
Pig, sheep and the most country of fowl, China Meat yield in 2006 is up to 80,510,000 tons, including more than 1,500 ten thousand tons of bones, it is seen that
Live stock and fowl bone is a huge resource, if it will cause have big waste using bad, or even pollution environment.If bone can be concentrated
Get up to be processed, can both turn waste into wealth, promote the development of food food and drink, need of the people to food nutrition can be met again
Ask.
At present, concentrated bone soup is mainly concentrated in vacuo using economic benefits and social benefits, and subject matter is that evaporation is higher using steam cost, is removed
The expense of 1 ton of water needs 60 yuan or so；By taking 100 tons of bone soup extract solutions as an example, raw material solid content is 5% or so, is concentrated to
30%, it is necessary to remove 83.3 tons of water, and such daily rate is 5000 yuan.
The content of the invention
In view of the above-mentioned problems, it is an object of the invention to provide a kind of system of the low concentrated bone soup low with production cost of energy consumption
Make technique and system.
To reach above-mentioned purpose, technical scheme proposed by the invention is：A kind of manufacture craft of concentrated bone soup, its feature
It is, comprises the steps：
Step 1 centrifugal filtration：Bone soup extract solution is filtered into obtain bone soup centrifugate after centrifugation grease separation；
Step 2 nanofiltration concentrates：By bone soup centrifugate after cartridge filter filters, 10-40bar is pressurized to through booster pump, is used
The concentration of bone soup is concentrated into 20-30% by the NF membrane of molecular cut off 50-200 dalton, obtains nanofiltration concentrate；
Step 3 is concentrated in vacuo：Nanofiltration concentrate into reduced vacuum double effect evaporator continue concentration the concentration of bone soup is dense
40%-60% is reduced to, obtains concentrated bone soup.
Preferably, 50-70 DEG C of temperature in step 2 NF membrane concentration process.
Preferably, pH=4-7 in step 2 NF membrane concentration process.
Preferably, in step 2 nanofiltration concentration process, in addition to nanofiltration concentrate is back to before booster pump circulate it is dense
The process of contracting.
Preferably, the centrifugation grease described in step 1 is separated into is centrifuged at a high speed through disc-type.
Preferably, the filtering accuracy of the cartridge filter described in step 2 is 1-10 μm.
Further, described centrifugation apparatus is disc-type supercentrifuge.
Preferably, the filtering accuracy of described cartridge filter is 1-10 μm.
Present invention additionally comprises a kind of manufacturing system of concentrated bone soup, it is characterised in that：Including passing through feed pipe successively phase
Centrifugation apparatus even, dehvery pump, cartridge filter, booster pump；Described booster pump connects high pressure resistant nanofiltration membrane component；Described
High pressure resistant nanofiltration membrane component includes the interior circularly-supercharged pump connected by pipeline and high pressure resistant nanofiltration membrane component, and described is high pressure resistant
By concentrate pipeline connection concentration flow container, dialyzate outlet is connected by dialyzate pipeline for the concentrate liquid outlet of nanofiltration membrane component
Connect dialysis fluid container；Described concentration flow container connection vacuum double effect evaporator.
Further, described high pressure resistant nanofiltration membrane component includes the first high pressure resistant nanofiltration membrane component and the second high pressure resistant nanofiltration
Membrane module, the described first high pressure resistant nanofiltration membrane component include by pipeline connection first in circularly-supercharged pump and the first resistance to height
Nanofiltration membrane component is pressed, the concentrate liquid outlet of the described first high pressure resistant nanofiltration membrane component is connected by the connection of the first concentrate pipeline
Concentration flow container is connect, dialyzate outlet connects dialysis fluid container by the first dialyzate pipeline；The second described high pressure resistant NF membrane group
Part is included by circularly-supercharged pump and the second high pressure resistant nanofiltration membrane component in the second of pipeline connection, and described second high pressure resistant receives
The concentrate liquid outlet of filter membrane component is saturating by second by the second concentrate pipeline connection connection concentration flow container, dialyzate outlet
Analyse liquid pipe road connection dialysis fluid container；Circularly-supercharged pump charging aperture connects booster pump and first by connecting pipe in described second
Pipeline between interior circularly-supercharged pump, and be interconnected between the first described concentrate pipeline and connecting pipe.
Preferably, the NF membrane that the high pressure resistant nanofiltration membrane component uses is tubular type, rolling, dish tubular type or flat knot
Structure, proof pressure 0-50bar.
Using above-mentioned technical proposal, the manufacture craft and system of concentrated bone soup of the present invention, can significantly reduce dense
The energy consumption of the making of contracting bone soup, Business Economic Benefit and social benefit are clearly.
Brief description of the drawings
Fig. 1 is the manufacturing system schematic diagram of concentrated bone soup of the present invention.
Embodiment
With reference to the accompanying drawings and detailed description, the present invention will be further described.
As shown in figure 1, the manufacturing system of concentrated bone soup of the present invention, including be sequentially connected by feed pipe 102
Centrifugation apparatus 101, dehvery pump 103, cartridge filter 104, booster pump 105；Booster pump 106 connects high pressure resistant NF membrane group
Part；High pressure resistant nanofiltration membrane component includes the first high pressure resistant 106 and second high pressure resistant nanofiltration membrane component 106` of nanofiltration membrane component, described
The first high pressure resistant nanofiltration membrane component 106 include that circularly-supercharged pump 1061 and first is high pressure resistant receives by the first of pipeline connection
Filter membrane component 1062, the concentrate liquid outlet of the described first high pressure resistant nanofiltration membrane component 1062 pass through the first concentrate pipeline
1061 connection connection concentration flow containers 107, dialyzate outlet connects dialysis fluid container 109 by the first dialyzate pipeline 1064；Second
High pressure resistant nanofiltration membrane component 106` include by pipeline connection second in the circularly-supercharged high pressure resistant NF membranes of pump 1061` and second
Element 1062`, the described second high pressure resistant nanofiltration membrane component 1062` concentrate liquid outlet pass through the second concentrate pipeline 1063
` connections connection concentration flow container 107, dialyzate outlet passes through the second dialyzate pipeline 1064` connections dialysis fluid container 109；In second
Circularly-supercharged pump 1061` charging apertures pass through between circularly-supercharged pump 1061 in connecting pipe 1065` connections booster pump 105 and first
Pipeline, and be interconnected between the first described concentrate pipeline 1063 and connecting pipe 1065`；Described concentration flow container 107 connects
Connect vacuum double effect evaporator 108；In addition, corresponding pipeline is provided with respective valves, this belongs to art technology general technology means,
It is not repeated herein., can be by changing the opening and closing of valve by setting the benefit of 2 groups of high pressure resistant nanofiltration membrane components to be
The serial or parallel connection concentration of 2 groups of high pressure resistant nanofiltration membrane components is realized, reaches the purpose that feed liquid further concentrates.
Further, centrifugation apparatus 101 is disc-type supercentrifuge.
Preferably, the filtering accuracy of cartridge filter 104 is 1-10 μm.
Preferably, the NF membrane that high pressure resistant nanofiltration membrane component 1062 uses is tubular type, rolling, dish tubular type or flat knot
Structure, proof pressure 0-50bar.
Embodiment 1
Step 1 centrifugal filtration：The extract solution 100KG that concentration is 5% is filtered into obtain bone soup centrifugate after centrifugation grease separation
99KG；
Step 2 nanofiltration concentrates：After the cartridge filter that the filtered precision of bone soup centrifugate is 1 μm is filtered, it is pressurized through booster pump
To 10-40bar, 50-70 DEG C of temperature is controlled in NF membrane concentration process, pH=4 are controlled in concentration process, using molecular cut off
The concentration of bone soup is concentrated into 20% by the NF membrane of 50 dalton, obtains nanofiltration concentrate；In nanofiltration concentration process, in addition to it will receive
Filter concentration liquid is back to the process for carrying out circulating concentration before booster pump；
Step 3 is concentrated in vacuo：Nanofiltration concentrate continues to be concentrated to give concentrated bone soup into reduced vacuum double effect evaporator
9.9KG, concentration 50%.
Embodiment 2
Step 1 centrifugal filtration：The extract solution that concentration is 4% is filtered into obtain bone soup centrifugate after centrifugation grease separation；
Step 2 nanofiltration concentrates：After the cartridge filter that the filtered precision of bone soup centrifugate is 5 μm is filtered, it is pressurized through booster pump
To 10-40bar, 50-70 DEG C of temperature is controlled in NF membrane concentration process, pH=6 are controlled in concentration process, using molecular cut off
The concentration of bone soup is concentrated into 26% by the NF membrane of 100 dalton, obtains nanofiltration concentrate；In nanofiltration concentration process, in addition to will
Nanofiltration concentrate is back to the process for carrying out circulating concentration before booster pump；
Step 3 is concentrated in vacuo：Nanofiltration concentrate continues to be concentrated to give concentrated bone soup into reduced vacuum double effect evaporator
7.6KG, concentration 52%.
Embodiment 3
Step 1 centrifugal filtration：The bone soup extract solution 100kg that concentration is 5% is filtered into obtain bone soup centrifugation after centrifugation grease separation
Liquid；
Step 2 nanofiltration concentrates：After the cartridge filter that the filtered precision of bone soup centrifugate is 10 μm is filtered, it is pressurized through booster pump
To 10-40bar, 50-70 DEG C of temperature is controlled in NF membrane concentration process, pH=7 are controlled in concentration process, using molecular cut off
The concentration of bone soup is concentrated into 30% by the NF membrane of 200 dalton, obtains nanofiltration concentrate；In nanofiltration concentration process, in addition to will
Nanofiltration concentrate is back to the process for carrying out circulating concentration before booster pump；
Step 3 is concentrated in vacuo：Nanofiltration concentrate continues to concentrate into reduced vacuum double effect evaporator, obtains concentrated bone soup
8.25KG, concentration 60%.
By contrast, concentrated bone soup is prepared using the technique and system of the present invention, product design can be concentrated to from 5%
30%, energy consumption can be significantly reduced；Film concentrated cost is 15 yuan per ton, and this includes film renewal cost, the electricity charge, cleaning agent, equipment dimension
Shield expense etc.；Calculated with producing 100 tons of extract solutions daily, can be saved by removing one ton of water by 45 yuan, remove within 1 day 83.3 tons, saving takes
With for 3748.5 yuan, calculated according to work in 330 days within 1 year, 123.7 ten thousand yuan of energy consumption can be saved every year；Business Economic Benefit and society
Meeting benefit is clearly.
Although specifically showing and describing the present invention with reference to preferred embodiment, those skilled in the art should be bright
In vain, do not departing from the spirit and scope of the present invention that appended claims are limited, in the form and details to this hair
It is bright to make a variety of changes, it is protection scope of the present invention.
Claims (10)
1. a kind of manufacture craft of concentrated bone soup, it is characterised in that comprise the steps：
Step 1 centrifugal filtration：Bone soup extract solution is filtered into obtain bone soup centrifugate after centrifugation grease separation；
Step 2 nanofiltration concentrates：By bone soup centrifugate after cartridge filter filters, 10-40bar is pressurized to through booster pump, is used
The concentration of bone soup is concentrated into 20-30% by the NF membrane of molecular cut off 50-200 dalton, obtains nanofiltration concentrate；
Step 3 is concentrated in vacuo：Nanofiltration concentrate into reduced vacuum double effect evaporator continue concentration the concentration of bone soup is dense
40%-60% is reduced to, obtains concentrated bone soup.
2. the manufacture craft of a kind of concentrated bone soup according to claim 1, it is characterised in that step 2 NF membrane is concentrated
50-70 DEG C of temperature in journey.
3. the manufacture craft of a kind of concentrated bone soup according to claim 1, it is characterised in that step 2 NF membrane is concentrated
PH=4-7 in journey.
A kind of 4. manufacture craft of concentrated bone soup according to claim 1, it is characterised in that step 2 nanofiltration concentration process
In, in addition to nanofiltration concentrate is back to the process for carrying out circulating concentration before booster pump.
A kind of 5. manufacture craft of concentrated bone soup according to claim 1, it is characterised in that the centrifugal oil described in step 1
Fat is separated into be centrifuged at a high speed through disc-type.
A kind of 6. manufacture craft of concentrated bone soup according to claim 1, it is characterised in that security personnel described in step 2
The filtering accuracy of filter is 1-10 μm.
A kind of 7. manufacturing system of concentrated bone soup, it is characterised in that：Including the centrifugation apparatus, defeated being sequentially connected by feed pipe
Expect pump, cartridge filter, booster pump；Described booster pump connects high pressure resistant nanofiltration membrane component；Described high pressure resistant NF membrane group
Part include by pipeline connection interior circularly-supercharged pump and high pressure resistant nanofiltration membrane component, described high pressure resistant nanofiltration membrane component it is dense
For the outlet of contracting liquid liquid by concentrate pipeline connection connection concentration flow container, dialyzate outlet connects dialyzate by dialyzate pipeline
Tank；Described concentration flow container connection vacuum double effect evaporator.
A kind of 8. manufacturing system of concentrated bone soup according to claim 7, it is characterised in that：Described high pressure resistant NF membrane
Component includes the first high pressure resistant nanofiltration membrane component and the second high pressure resistant nanofiltration membrane component, the described first high pressure resistant nanofiltration membrane component
Including connected by pipeline first in circularly-supercharged pump and the first high pressure resistant nanofiltration membrane component, the described first high pressure resistant nanofiltration
By the first concentrate pipeline connection connection concentration flow container, dialyzate outlet passes through the first dialysis for the concentrate liquid outlet of membrane component
Liquid pipe road connects dialysis fluid container；The second described high pressure resistant nanofiltration membrane component include by pipeline connection second in it is circularly-supercharged
Pump and the second high pressure resistant nanofiltration membrane component, the concentrate liquid outlet of the described second high pressure resistant nanofiltration membrane component pass through the second concentration
Liquid pipe road connection connection concentration flow container, dialyzate outlet connects dialysis fluid container by the second dialyzate pipeline；In described second
Circularly-supercharged pump charging aperture connects the pipeline in booster pump and first between circularly-supercharged pump, and described first by connecting pipe
It is interconnected between concentrate pipeline and connecting pipe.
A kind of 9. manufacturing system of concentrated bone soup according to claim 7 or 8, it is characterised in that described centrifugation apparatus
For disc-type supercentrifuge；The filtering accuracy of described cartridge filter is 1-10 μm.
A kind of 10. manufacturing system of concentrated bone soup according to claim 7 or 8, it is characterised in that the high pressure resistant nanofiltration
The NF membrane that membrane component uses is tubular type, rolling, dish tubular type or plate armature, proof pressure 0-50bar.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711058526.5A CN107637821A (en) | 2017-11-01 | 2017-11-01 | The manufacture craft and system of a kind of concentrated bone soup |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711058526.5A CN107637821A (en) | 2017-11-01 | 2017-11-01 | The manufacture craft and system of a kind of concentrated bone soup |
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| CN107637821A true CN107637821A (en) | 2018-01-30 |
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| CN201711058526.5A Pending CN107637821A (en) | 2017-11-01 | 2017-11-01 | The manufacture craft and system of a kind of concentrated bone soup |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN108774582A (en) * | 2018-06-12 | 2018-11-09 | 合肥丰洁生物科技有限公司 | A kind of film condensing device for plant oil extract |
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