CN208318168U - A kind of manufacturing system of concentrated bone soup - Google Patents
A kind of manufacturing system of concentrated bone soup Download PDFInfo
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- CN208318168U CN208318168U CN201721438246.2U CN201721438246U CN208318168U CN 208318168 U CN208318168 U CN 208318168U CN 201721438246 U CN201721438246 U CN 201721438246U CN 208318168 U CN208318168 U CN 208318168U
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- nanofiltration membrane
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Abstract
The utility model discloses a kind of manufacturing systems of concentrated bone soup, it is characterised in that: including centrifugation apparatus, dehvery pump, cartridge filter, the booster pump being sequentially connected by feed pipe；The booster pump connects high pressure resistant nanofiltration membrane component；The high pressure resistant nanofiltration membrane component includes by circularly-supercharged pump and high pressure resistant nanofiltration membrane component in pipeline connection, by concentrate pipeline connection concentration flow container, dialyzate outlet connects dialysis fluid container by dialyzate pipeline for the concentrate liquid outlet of the high pressure resistant nanofiltration membrane component；The concentration flow container connects vacuum double effect evaporator.The energy consumption of the production of concentrated bone soup can be significantly reduced in the manufacturing system of concentrated bone soup described in the utility model, and Business Economic Benefit and social benefit are clearly.
Description
Technical field
The utility model relates to concentrated bone soup field, in particular to a kind of manufacturing system of concentrated bone soup.
Background technique
Live stock and fowl bone is a kind of very high meat by- product of nutritive value, it contains, and there are many nutrition necessary to human body
Ingredient, such as protein, fatty acid, Phospholipids, phosphorus unit chondroitin, ossein, multivitamin.China is feeding 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 will cause the waste for having big, or even pollution environment using bad.If bone can be concentrated
Get up to be processed, can both turn waste into wealth, push the development of food food and drink, and can satisfy people to the need of food nutrition
It asks.
Currently, concentrated bone soup mainly uses economic benefits and social benefits to be concentrated in vacuo, main problem is that evaporation is higher using steam cost, removal
The expense of 1 ton of water needs 60 yuan or so；By taking 100 tons of bone soup extracting solutions as an example, raw material solid content is 5% or so, is concentrated to
30%, need to remove 83.3 tons of water, such daily rate is 5000 yuan.
Utility model content
In view of the above-mentioned problems, the purpose of this utility model is to provide the systems for the concentrated bone soup that low energy consumption, production cost is low
Make system.
In order to achieve the above objectives, the technical solution that the utility model is proposed are as follows: a kind of manufacturing system of concentrated bone soup,
It is characterized in that: including centrifugation apparatus, dehvery pump, cartridge filter, the booster pump being sequentially connected by feed pipe；The increasing
Press pump connects high pressure resistant nanofiltration membrane component；The high pressure resistant nanofiltration membrane component includes by circularly-supercharged pump in pipeline connection
Concentrate liquid outlet with high pressure resistant nanofiltration membrane component, the high pressure resistant nanofiltration membrane component passes through the connection concentration of concentrate pipeline
Flow container, dialyzate outlet connect dialysis fluid container by dialyzate pipeline；The concentration flow container connects vacuum double effect evaporator.
Further, the 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 high pressure resistant nanofiltration membrane component of described first include circularly-supercharged pump and the first resistance to height in first connected by pipeline
Nanofiltration membrane component is pressed, the concentrate liquid outlet of the high pressure resistant nanofiltration membrane component of described first 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 high pressure resistant nanofiltration membrane group of described second
Part includes circularly-supercharged pump and the second high pressure resistant nanofiltration membrane component in second connected by pipeline, and described second is high pressure resistant to be received
The concentrate liquid outlet of filter membrane component connects connection concentration flow container by the second concentrate pipeline, and dialyzate outlet is saturating by second
It analyses liquid pipe road and connects dialysis fluid container；Circularly-supercharged pump feed inlet connects booster pump and first by connecting pipe in described second
Pipeline between interior circularly-supercharged pump, and be interconnected between the first concentrate pipeline and connecting pipe.
Further, the centrifugation apparatus is disc-type supercentrifuge.
Preferably, the filtering accuracy of the cartridge filter is 1-10 μm.
Preferably, the nanofiltration 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.
By adopting the above technical scheme, concentration can be significantly reduced in the manufacturing system of concentrated bone soup described in the utility model
The energy consumption of the production of bone soup, Business Economic Benefit and social benefit are clearly.
Detailed description of the invention
Fig. 1 is the manufacturing system schematic diagram of concentrated bone soup described in the utility model.
Specific embodiment
With reference to the accompanying drawings and detailed description, the utility model is described further.
As shown in Figure 1, the manufacturing system of concentrated bone soup described in the utility model, including successively by feed pipe 102
Connected centrifugation apparatus 101, dehvery pump 103, cartridge filter 104, booster pump 105；Booster pump 106 connects high pressure resistant nanofiltration membrane
Component；High pressure resistant nanofiltration membrane component includes the first high pressure resistant nanofiltration membrane component 106 and the second high pressure resistant nanofiltration membrane component 106`, institute
The high pressure resistant nanofiltration membrane component 106 of first stated includes circularly-supercharged pump 1061 and first high pressure resistant in first connected by pipeline
The concentrate liquid outlet of nanofiltration membrane component 1062, the high pressure resistant nanofiltration membrane component 1062 of described first passes 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` includes the circularly-supercharged high pressure resistant nanofiltration membrane of pump 1061` and second in second connected by pipeline
The concentrate liquid outlet of element 1062`, the high pressure resistant nanofiltration membrane component 1062` of described second pass through the second concentrate pipeline 1063
` connection connection concentration flow container 107, dialyzate outlet passes through the second dialyzate pipeline 1064` connection dialysis fluid container 109；In second
Circularly-supercharged pump 1061` feed inlet passes through between pump 1061 circularly-supercharged in connecting pipe 1065` connection booster pump 105 and first
Pipeline, and be interconnected between the first concentrate pipeline 1063 and connecting pipe 1065`；The concentration flow container 107 connects
Connect vacuum double effect evaporator 108；In addition, corresponding pipeline is equipped with respective valves, this belongs to art technology general technology means,
It is not repeated herein.Benefit by the way that 2 groups of high pressure resistant nanofiltration membrane components are arranged is can to pass through the opening and closing of replacement valve
The serial or parallel connection concentration for realizing 2 groups of high pressure resistant nanofiltration membrane components, achievees the purpose that feed liquid is further concentrated.
Further, centrifugation apparatus 101 is disc-type supercentrifuge.
Preferably, the filtering accuracy of cartridge filter 104 is 1-10 μm.
Preferably, the nanofiltration 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 extracting solution 100KG that concentration is 5% is filtered into obtain bone soup centrifugate after centrifugation grease separation
99KG；
Step 2 nanofiltration concentration: by bone soup centrifugate after the cartridge filter filtering that filtering accuracy is 1 μm, through booster pump
It is pressurized to 10-40bar, 50-70 DEG C of temperature is controlled in nanofiltration membrane concentration process, pH=4 are controlled in concentration process, using retention point
The concentration of bone soup is concentrated into 20% by the nanofiltration membrane of son 50 dalton of amount, obtains nanofiltration concentrate；In nanofiltration concentration process, further include
Nanofiltration concentrate is back to the process that circulation concentration is carried out before booster pump；
Step 3 vacuum concentration: nanofiltration concentrate enters reduced vacuum double effect evaporator and continues to be concentrated to give concentrated bone soup
9.9KG, concentration 50%.
Embodiment 2
Step 1 centrifugal filtration: the extracting solution that concentration is 4% is filtered into obtain bone soup centrifugate after centrifugation grease separation；
Step 2 nanofiltration concentration: by bone soup centrifugate after the cartridge filter filtering that filtering accuracy is 5 μm, through booster pump
It is pressurized to 10-40bar, 50-70 DEG C of temperature is controlled in nanofiltration membrane concentration process, pH=6 are controlled in concentration process, using retention point
The concentration of bone soup is concentrated into 26% by the nanofiltration membrane of son 100 dalton of amount, obtains nanofiltration concentrate；In nanofiltration concentration process, also wrap
Include the process that nanofiltration concentrate is back to and carries out circulation concentration before booster pump；
Step 3 vacuum concentration: nanofiltration concentrate enters reduced vacuum double effect evaporator and continues to be concentrated to give concentrated bone soup
9.9KG, concentration 40%.
Embodiment 3
Step 1 centrifugal filtration: by concentration be 5% bone soup extracting solution 100kg through centrifugation grease separation after filter bone soup from
Heart liquid；
Step 2 nanofiltration concentration: by bone soup centrifugate after the cartridge filter filtering that filtering accuracy is 10 μm, through booster pump
It is pressurized to 10-40bar, 50-70 DEG C of temperature is controlled in nanofiltration membrane concentration process, pH=7 are controlled in concentration process, using retention point
The concentration of bone soup is concentrated into 30% by the nanofiltration membrane of son 200 dalton of amount, obtains nanofiltration concentrate；In nanofiltration concentration process, also wrap
Include the process that nanofiltration concentrate is back to and carries out circulation concentration before booster pump；
Step 3 vacuum concentration: nanofiltration concentrate enters reduced vacuum double effect evaporator and continues to be concentrated, and obtains concentrated bone soup
8.25KG, concentration 60%.
By contrast, concentrated bone soup is prepared using the technique of the utility model and system, product design can be concentrated from 5%
To 30%, energy consumption can be significantly reduced；Film concentrated cost is 15 yuan per ton, this includes film renewal cost, the electricity charge, cleaning agent, equipment
Maintenance cost etc.；To produce 100 tons of extracting solution calculations daily, can be saved by removing one ton of water by 45 yuan, removed 83.3 tons within 1 day, saved
Expense is 3748.5 yuan, is calculated according to work in 330 days within 1 year, every year can be 123.7 ten thousand yuan with energy saving；Business Economic Benefit and
Social benefit is clearly.
Although specifically showing and describing the utility model in conjunction with preferred embodiment, those skilled in the art is answered
This is understood, in the spirit and scope for not departing from the utility model defined by the appended claims, in form and details
On the utility model is made a variety of changes, be the protection scope of the utility model.
Claims (5)
1. a kind of 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；The booster pump connects high pressure resistant nanofiltration membrane component；The high pressure resistant nanofiltration membrane group
Part include by pipeline connection in it is circularly-supercharged pump and high pressure resistant nanofiltration membrane component, the 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；The concentration flow container connects vacuum double effect evaporator.
2. a kind of manufacturing system of concentrated bone soup according to claim 1, it is characterised in that: the high pressure resistant nanofiltration membrane
Component includes the first high pressure resistant nanofiltration membrane component and the second high pressure resistant nanofiltration membrane component, the high pressure resistant nanofiltration membrane component of described first
Including connected by pipeline first in it is circularly-supercharged pump and the first high pressure resistant nanofiltration membrane component, the high pressure resistant nanofiltration of described first
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 high pressure resistant nanofiltration membrane component of described second includes circularly-supercharged in second connected by pipeline
The concentrate liquid outlet of pump and the second high pressure resistant nanofiltration membrane component, the high pressure resistant nanofiltration membrane component of described second passes 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 feed inlet 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.
3. a kind of manufacturing system of concentrated bone soup according to claim 1 or 2, which is characterized in that the centrifugation apparatus
For disc-type supercentrifuge.
4. a kind of manufacturing system of concentrated bone soup according to claim 1 or 2, which is characterized in that security personnel's filtering
The filtering accuracy of device is 1-10 μm.
5. a kind of manufacturing system of concentrated bone soup according to claim 1 or 2, which is characterized in that the high pressure resistant nanofiltration
The nanofiltration membrane that membrane component uses is tubular type, rolling, dish tubular type or plate armature, proof pressure 0-50bar.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721438246.2U CN208318168U (en) | 2017-11-01 | 2017-11-01 | A kind of manufacturing system of concentrated bone soup |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201721438246.2U CN208318168U (en) | 2017-11-01 | 2017-11-01 | A kind of manufacturing system of concentrated bone soup |
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| CN208318168U true CN208318168U (en) | 2019-01-04 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107637821A (en) * | 2017-11-01 | 2018-01-30 | 同舟纵横（厦门）流体技术有限公司 | The manufacture craft and system of a kind of concentrated bone soup |
-
2017
- 2017-11-01 CN CN201721438246.2U patent/CN208318168U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107637821A (en) * | 2017-11-01 | 2018-01-30 | 同舟纵横（厦门）流体技术有限公司 | The manufacture craft and system of a kind of concentrated bone soup |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: A production system of concentrated bone soup Effective date of registration: 20210205 Granted publication date: 20190104 Pledgee: Xiamen Huli District Financing Guarantee Co.,Ltd. Pledgor: CROSSFLOW (XIAMEN) FLUID TECHNOLOGY Co.,Ltd. Registration number: Y2021980001060 |
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| PE01 | Entry into force of the registration of the contract for pledge of patent right |