CN105434504A - Fat emulsion tail liquid treatment apparatus and method thereof - Google Patents
Fat emulsion tail liquid treatment apparatus and method thereof Download PDFInfo
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- CN105434504A CN105434504A CN201410439291.4A CN201410439291A CN105434504A CN 105434504 A CN105434504 A CN 105434504A CN 201410439291 A CN201410439291 A CN 201410439291A CN 105434504 A CN105434504 A CN 105434504A
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Abstract
The invention discloses a fat emulsion tail liquid treatment apparatus and a method thereof, and belongs to the field of fat emulsion preparation. The treatment system comprises a colostrum tank, a homogenizing tank, a transfer pump and a homogenizer, the colostrum tank, the homogenizing tank, the transfer pump and the homogenizer are connected by a pipeline and valves arranged on the pipeline to form a circulating system, and the transfer pump is serially connected with the homogenizer, and is further serially connected with the colostrum tank, the homogenizing tank which are connected in parallel. The tail liquid treatment method sequentially comprises the following steps: forming self circulation among the colostrum tank, the transfer pump and the homogenizer; pumping fat emulsion in the colostrum tank to the homogenizing tank through the transfer pump and the homogenizer; pumping the fat emulsion in the homogenizing tank to the colostrum tank through the transfer pump and the homogenizer; pumping the fat emulsion in the colostrum tank to the homogenizing tank through the transfer pump and the homogenizer; and allowing the fat emulsion in the homogenizing tank to enter an external subsequent technology. The fat emulsion tail liquid treatment apparatus and the method thereof greatly reduce the tail liquid discharge amount on the premise of guaranteeing safety and reliability.
Description
Technical field
The invention belongs to fat milk preparation field.
Background technology
Fat milk is a kind of not only even but also stable lipomul be made up of refined soybean oil and refined lecithin, provides high-energy and required fatty acid under the importance that its is treated is non-bowel provisions.Proved that the fat that human body is taken in first forms Chylomicron through gastrointestinal absorption from physiology and threpsology, and the form of these product is all extremely similar to chyle with composition, directly to the venous patient infusion that can not take food, can provide lipid nutrition.
Fat milk tail washings treatment process ensures product quality, ensures that homogenizer equipment normally runs, reduce the important evidence of production cost, and domestic existing fat milk tail washings treatment process is as follows:
1, fat milk tail washings all discharges, and does not reclaim.Advantage: ensure product quality; Shortcoming: loss is large, by often criticizing medicine homogenizing 6 times, each discharge 20 kilograms, within one day, produce 10 batches, one day loss: 20*6*10=1200 kilogram, bottled with 250ML, loss: 4800 bottles, with every bottle of 10 yuan of cost prices, a loss in month: 4800*10*30=1440000 unit.
2, fat milk tail washings centralized recovery, the every homogenizing of fat milk once, concentrate and be discharged into a storage tank by tail washings, finally carries out homogenizing to the medicinal liquid that storage tank reclaims by production technology, last fill separately.By every day by production 10 batches, often criticize homogenizing 6 times, be tail washings 20 kilograms at every turn, within one day, reclaims altogether: 20*6*10=1200 kilogram.But tail washings is concentrated and is discharged into a storage tank and operates extremely difficult in process of production, be difficult to ensure product quality, and mix because often criticizing tail washings, and the storage time being long, there is great quality risk in such product.
Summary of the invention
The object of the invention is to: under proposing the safe and reliable prerequisite of a kind of guarantee, significantly reduce fat milk tail washings blood processor and the method thereof of tail liquid emissions amount.
The object of the invention is realized by following technical proposals:
A kind of fat milk tail washings processing system, comprise colostrum tank, homogenizing tank and delivery pump and homogenizer, described colostrum tank, homogenizing tank, delivery pump and homogenizer are communicated with by pipeline and upper valve thereof and form blood circulation, described delivery pump is connected with homogenizer, and be connected in series with the colostrum tank be in parallel and homogenizing tank further, and colostrum tank is communicated with the arrival end of delivery pump with the port of export of homogenizing tank, the port of export of homogenizer is communicated with the arrival end of colostrum tank with homogenizing tank respectively, pipeline between the described delivery pump port of export and homogenizing tank arrival end is also provided with branch road and the ft connection of band the 10th valve, the port of export of described colostrum tank and homogenizing tank is also respectively equipped with band the 2nd, the branch road of 7 valves and ft connection, the arrival end of described colostrum tank and homogenizing tank is respectively equipped with the 12nd, 9 valves, pipeline between the port of export of described colostrum tank and homogenizing tank and the arrival end of delivery pump is respectively equipped with the 4th, 5 valves, described colostrum tank and homogenizing tank are also equipped with tail washings amount supervising device in it, and the 4th valve is electrically connected with the tail washings supervising device of described homogenizing tank and the tail washings amount signal that can provide according to it controls aperture, 5th valve is electrically connected with the tail washings supervising device of described colostrum tank and the tail washings amount signal that can provide according to it controls aperture.
As selection, the port of export of described colostrum tank is provided with the 1st valve, and the port of export of described homogenizing tank is provided with the 8th valve.
As further selection, the pipeline between described 1st valve and the 4th valve is also provided with the 3rd valve, and the 1st, 2, be communicated with by threeway between 3 valves; Pipeline between described 8th valve and the 5th valve is also provided with the 6th valve, and the 6th, 7, be communicated with by threeway between 8 valves.
As selection, the pipeline between described 12nd valve and the 9th valve is also provided with the 11st valve, and the 11st, be communicated with by threeway between 12 valves and homogenizer, the 9th, 10, be communicated with by threeway between 11 valves.
Adopt a method for aforementioned fat milk tail washings processing system process tail washings, comprise the following steps successively:
1) make colostrum tank, between delivery pump and homogenizer, form self-loopa;
2) self-loopa is disconnected, fat milk in colostrum tank is made to pump into homogenizing tank through delivery pump and homogenizer, and when fat milk in colostrum tank is reduced to default tail washings amount the 4th, 5 valves are adjusted to default aperture automatically, from colostrum tank and homogenizing tank, extract fat milk pumps into homogenizing tank through delivery pump and homogenizer simultaneously;
3) when in colostrum tank, tail washings is reduced to predetermined limit amount, close the 4th valve, the 5th valve wide open makes homogenizing tank, forms self-loopa between delivery pump and homogenizer, opens the 2nd valve and drains colostrum tank tail washings, carry out fast processing to colostrum tank;
4) the 2nd valve is closed, disconnect self-loopa, fat milk in homogenizing tank is made to pump into colostrum tank through delivery pump and homogenizer, and when fat milk in homogenizing tank is reduced to described default tail washings amount the 4th, 5 valves are adjusted to contrary described default aperture automatically, from colostrum tank and homogenizing tank, extract fat milk pumps into colostrum tank through delivery pump and homogenizer simultaneously;
5) when in homogenizing tank, tail washings is reduced to described predetermined limit amount, close the 5th valve, the 4th valve wide open makes colostrum tank, forms self-loopa between delivery pump and homogenizer, opens the 7th valve and drains homogenizing tank tail washings, carry out fast processing to homogenizing tank;
6) disconnect self-loopa, make fat milk in colostrum tank pump into homogenizing tank through delivery pump and homogenizer;
7) in homogenizing tank, the branch road of fat milk band the 10th valve enters outside subsequent technique.
In such scheme, no matter be different cultivars, specification Emulsion, can by homogenizing process repeatedly, continuous seepage can ensure that pressure stability, Emulsion quality are good, efficiency is high thus.
As selection, also comprise at least one order 2 step between described 5th step and the 6th step to the 5th step.
In such scheme, according to refined lecithin content in fat milk, and the requirement such as the quality of production, can carry out further repeatedly back and forth repeatedly.
As selection, described default tail washings amount is that in colostrum tank, fat milk pumps into through delivery pump and homogenizer the minimum tail washings amount that homogenizer in homogenizing tank process does not enter gas, and described predetermined limit amount is the 4th, the total flow of 5 valves meets the minimum tail washings amount that homogenizer does not enter gas.
In such scheme, in order to ensure producing safely and reliably, meeting the traffic requirement of homogenizer, limiting all via the 4th valve, and while the minimum tail washings amount of not bringing gas into via the 4th, when 5 valves enter homogenizer.
As further selection, described default tail washings amount is 20 kilograms, and described predetermined limit amount is 1 kilogram.
As selection, described default aperture is under the maximum prerequisite of satisfied 4th valve flow, the 4th, the total flow of 5 valves meets the maximum opening that homogenizer does not enter gas.
In such scheme, homogenizing tank can be made can not to flow backwards to colostrum tank when satisfied 4th valve flow is maximum, in colostrum tank, tail washings can extract complete as soon as possible simultaneously, raises the efficiency; 4th, the total flow of 5 valves meets the maximum opening that homogenizer does not enter gas, both ensure that the traffic requirement of the safe and reliable operation of homogenizer, and has met the highest operational efficiency again.Wherein, contrary described default aperture, refers to the 4th, 5 valves presets aperture and exchange, and namely the 4th valve is preset aperture and is adjusted to former 5th valve and presets aperture, and similarly the 5th valve is preset aperture and is adjusted to former 4th valve and presets aperture.
As further selection, it is that to preset aperture be 33% to the 16%, 5th valve that described 4th valve presets aperture.
Aforementioned main formula case of the present invention and each further selection scheme thereof can independent assortment to form multiple scheme; be the present invention can adopt and claimed scheme: as the present invention; each selection can select combination in any with other; those skilled in the art can understand there is multiple combination according to prior art and common practise after understanding the present invention program; be the claimed technical scheme of the present invention, do not do exhaustive at this.
Beneficial effect of the present invention:
1, safe and reliable, stop the quality risk that fat milk tail washings exists in transport process.
2, fat milk tail washings amount is reduced, the final fat breast tail washings amount using the present invention to discharge is minimum reaches 1 kilogram, greatly reduce production cost like this, by often criticizing medicine homogenizing 6 times, each discharge 1 kilogram, within one day, produce 10 batches, one day loss: 1*6*10=60 kilogram, bottled with 250ML, loss: 120 bottles, with every bottle of 10 yuan of cost prices, a loss in month: 120*10*30=36000 unit.Minimizing: 1440000-36000=1304000 unit compared with concentrated emission treatment fat milk tail washings technique.
Accompanying drawing explanation
Fig. 1 is the device schematic flow sheet of the embodiment of the present invention;
1 be colostrum tank, 2 be wherein homogenizing tank, 3 be homogenizer, 4 for delivery pump.
Detailed description of the invention
Following non-limiting examples is for illustration of the present invention.
As shown in Figure 1, a kind of fat milk tail washings processing system, comprise colostrum tank 1, homogenizing tank 2 and delivery pump 4 and homogenizer 3, colostrum tank 1, homogenizing tank 2, delivery pump 4 and homogenizer 3 are communicated with by pipeline and upper valve thereof and form blood circulation, delivery pump 4 is connected with homogenizer 3, and be connected in series with the colostrum tank 1 be in parallel and homogenizing tank 2 further, and colostrum tank 1 is communicated with the arrival end of delivery pump 4 with the port of export of homogenizing tank 2, the port of export of homogenizer 3 is communicated with the arrival end of colostrum tank 1 with homogenizing tank 2 respectively, pipeline between delivery pump 4 port of export and homogenizing tank 2 arrival end is also provided with branch road and the ft connection of band the 10th valve, the port of export of colostrum tank 1 and homogenizing tank 2 is also respectively equipped with band the 2nd, the branch road of 7 valves and ft connection, the arrival end of colostrum tank 1 and homogenizing tank 2 is respectively equipped with the 12nd, 9 valves, pipeline between the port of export of colostrum tank 1 and homogenizing tank 2 and the arrival end of delivery pump 4 is respectively equipped with the 4th, 5 valves, colostrum tank 1 and homogenizing tank 2 are also equipped with tail washings amount supervising device in it, and the 4th valve is electrically connected with the tail washings supervising device of homogenizing tank 2 and the tail washings amount signal that can provide according to it controls aperture, 5th valve is electrically connected with the tail washings supervising device of colostrum tank 1 and the tail washings amount signal that can provide according to it controls aperture.As selection, as shown in this embodiment, the port of export of colostrum tank 1 is provided with the 1st valve, and the port of export of homogenizing tank 2 is provided with the 8th valve.Pipeline between 1st valve and the 4th valve is also provided with the 3rd valve, and the 1st, 2, be communicated with by threeway between 3 valves; Pipeline between 8th valve and the 5th valve is also provided with the 6th valve, and the 6th, 7, be communicated with by threeway between 8 valves.Pipeline between 12nd valve and the 9th valve is also provided with the 11st valve, and the 11st, be communicated with by threeway between 12 valves and homogenizer 3, the 9th, 10, be communicated with by threeway between 11 valves.
Adopt a method for aforementioned fat milk tail washings processing system process tail washings, comprise the following steps successively:
1) make colostrum tank 1, between delivery pump 4 and homogenizer 3, form self-loopa;
2) self-loopa is disconnected, fat milk in colostrum tank 1 is made to pump into homogenizing tank 2 through delivery pump 4 and homogenizer 3, and when fat milk in colostrum tank 1 is reduced to default tail washings amount the 4th, 5 valves are adjusted to default aperture automatically, from colostrum tank 1 and homogenizing tank 2, extract fat milk pumps into homogenizing tank 2 through delivery pump 4 and homogenizer 3 simultaneously;
3) when in colostrum tank 1, tail washings is reduced to predetermined limit amount, close the 4th valve, the 5th valve wide open makes homogenizing tank 2, forms self-loopa between delivery pump 4 and homogenizer 3, opens the 2nd valve and drains colostrum tank 1 tail washings, carry out fast processing to colostrum tank 1;
4) the 2nd valve is closed, disconnect self-loopa, fat milk in homogenizing tank 2 is made to pump into colostrum tank 1 through delivery pump 4 and homogenizer 3, and when fat milk in homogenizing tank 2 is reduced to default tail washings amount the 4th, 5 valves are automatically adjusted to and preset aperture on the contrary, from colostrum tank 1 and homogenizing tank 2, extract fat milk pumps into colostrum tank 1 through delivery pump 4 and homogenizer 3 simultaneously;
5) when in homogenizing tank 2, tail washings is reduced to predetermined limit amount, close the 5th valve, the 4th valve wide open makes colostrum tank 1, forms self-loopa between delivery pump 4 and homogenizer 3, opens the 7th valve and drains homogenizing tank 2 tail washings, carry out fast processing to homogenizing tank 2;
6) disconnect self-loopa, make fat milk in colostrum tank 1 pump into homogenizing tank 2 through delivery pump 4 and homogenizer 3;
7) in homogenizing tank 2, the branch road of fat milk band the 10th valve enters outside subsequent technique, as finished product operation.
As selection, presetting tail washings amount is that in colostrum tank 1, fat milk pumps into through delivery pump 4 and homogenizer 3 the minimum tail washings amount that homogenizer 3 in homogenizing tank 2 process does not enter gas, and predetermined limit amount is the 4th, the total flow of 5 valves meets the minimum tail washings amount that homogenizer 3 does not enter gas.As shown in this embodiment, presetting tail washings amount is 20 kilograms, and predetermined limit amount is 1 kilogram.Default aperture is under the maximum prerequisite of satisfied 4th valve flow, the 4th, the total flow of 5 valves meets the maximum opening that homogenizer 3 does not enter gas.As shown in this embodiment, the 4th valve presets aperture is that to preset aperture be 33% to the 16%, 5th valve.
According to refined lecithin content in fat milk, and the requirement such as the quality of production, can carry out further repeatedly back and forth repeatedly: also carry out between the 5th step and the 6th step at least one times the 2nd step to the technological operation of the 5th step.
For system shown in Figure 1, concrete operations example is as follows:
Homogenizing is carried out to colostrum tank 1 fat milk, first open the 1st, 3,4,12 valves, open delivery pump 4, homogenizer 3, make fat milk form self-circulation system through delivery pump 4, homogenizer 3, pipeline, start again to carry out adjust blood pressure to homogenizer 3, open the 11st simultaneously, 9 valves, close the 12nd valve, the minimizing of colostrum tank 1 tail washings weight monitored automatically by colostrum tank 1 tail washings amount supervising device, when 1, colostrum tank residue presets tail washings amount 20 kilograms, be just fat milk tail washings.Now the 5th valve is automatically adjusted to default aperture the 33%, 4th valve and is automatically adjusted to default aperture 16%, opens the 8th, 6 valves.When colostrum tank 1 tail washings weight reaches predetermined limit amount 1 kilogram, the 5th valve standard-sized sheet, simultaneously and close the 3rd, 4 valves.Open the 2nd valve and drain tail washings in colostrum tank 1 and pipeline thereof, fast processing is carried out to colostrum tank 1, complete rear closedown the 1st, 2 valves, open the 12nd valve, close the 11st, 9 valves, the fat milk of homogenizing tank 2 is made to transfer to colostrum tank 1, the minimizing of homogenizing tank 2 tail washings weight monitored automatically by homogenizing tank 2 tail washings amount supervising device, when the fat milk of homogenizing tank 2 reduces to default tail washings amount 20 kilograms, be just fat milk tail washings, 4th valve is automatically adjusted to default aperture the 33%, 5th valve and is automatically adjusted to default aperture 16%.Open the 1st, 3 valves, when homogenizing tank 2 tail washings weight is predetermined limit amount 1 kilogram, the 4th valve standard-sized sheet, simultaneously and close the 6th, 5 valves.Open the 7th valve and drain tail washings in homogenizing tank 2 and pipeline thereof, fast processing is carried out to homogenizing tank 2, complete rear closedown the 8th, 7 valves, open the 11st, 9 valves, close the 12nd valve, make the fat milk of colostrum tank 1 transfer to homogenizing tank 2.In last homogenizing tank 2, the branch road of fat milk band the 10th valve enters outside finished product operation.
The foregoing is only preferred embodiment of the present invention, not in order to limit the present invention, all any amendments done within the spirit and principles in the present invention, equivalent replacement and improvement etc., all should be included within protection scope of the present invention.
Claims (10)
1. a fat milk tail washings processing system, it is characterized in that comprising colostrum tank, homogenizing tank and delivery pump and homogenizer, described colostrum tank, homogenizing tank, delivery pump and homogenizer are communicated with by pipeline and upper valve thereof and form blood circulation, described delivery pump is connected with homogenizer, and be connected in series with the colostrum tank be in parallel and homogenizing tank further, and colostrum tank is communicated with the arrival end of delivery pump with the port of export of homogenizing tank, the port of export of homogenizer is communicated with the arrival end of colostrum tank with homogenizing tank respectively, pipeline between the described delivery pump port of export and homogenizing tank arrival end is also provided with branch road and the ft connection of band the 10th valve, the port of export of described colostrum tank and homogenizing tank is also respectively equipped with band the 2nd, the branch road of 7 valves and ft connection, the arrival end of described colostrum tank and homogenizing tank is respectively equipped with the 12nd, 9 valves, pipeline between the port of export of described colostrum tank and homogenizing tank and the arrival end of delivery pump is respectively equipped with the 4th, 5 valves, described colostrum tank and homogenizing tank are also equipped with tail washings amount supervising device in it, and the 4th valve is electrically connected with the tail washings supervising device of described homogenizing tank and the tail washings amount signal that can provide according to it controls aperture, 5th valve is electrically connected with the tail washings supervising device of described colostrum tank and the tail washings amount signal that can provide according to it controls aperture.
2. fat milk tail washings processing system as claimed in claim 1, it is characterized in that: the port of export of described colostrum tank is provided with the 1st valve, the port of export of described homogenizing tank is provided with the 8th valve.
3. fat milk tail washings processing system as claimed in claim 2, is characterized in that: the pipeline between described 1st valve and the 4th valve is also provided with the 3rd valve, and the 1st, 2, be communicated with by threeway between 3 valves; Pipeline between described 8th valve and the 5th valve is also provided with the 6th valve, and the 6th, 7, be communicated with by threeway between 8 valves.
4. fat milk tail washings processing system as claimed in claim 1, it is characterized in that: the pipeline between described 12nd valve and the 9th valve is also provided with the 11st valve, and the 11st, be communicated with by threeway between 12 valves and homogenizer, the 9th, 10, be communicated with by threeway between 11 valves.
5. adopt a method for the fat milk tail washings processing system process tail washings in Claims 1-4 described in arbitrary claim, it is characterized in that comprising the following steps successively:
1) make colostrum tank, between delivery pump and homogenizer, form self-loopa;
2) self-loopa is disconnected, fat milk in colostrum tank is made to pump into homogenizing tank through delivery pump and homogenizer, and when fat milk in colostrum tank is reduced to default tail washings amount the 4th, 5 valves are adjusted to default aperture automatically, from colostrum tank and homogenizing tank, extract fat milk pumps into homogenizing tank through delivery pump and homogenizer simultaneously;
3) when in colostrum tank, tail washings is reduced to predetermined limit amount, close the 4th valve, the 5th valve wide open makes homogenizing tank, forms self-loopa between delivery pump and homogenizer, opens the 2nd valve and drains colostrum tank tail washings, carry out fast processing to colostrum tank;
4) the 2nd valve is closed, disconnect self-loopa, fat milk in homogenizing tank is made to pump into colostrum tank through delivery pump and homogenizer, and when fat milk in homogenizing tank is reduced to described default tail washings amount the 4th, 5 valves are adjusted to contrary described default aperture automatically, from colostrum tank and homogenizing tank, extract fat milk pumps into colostrum tank through delivery pump and homogenizer simultaneously;
5) when in homogenizing tank, tail washings is reduced to described predetermined limit amount, close the 5th valve, the 4th valve wide open makes colostrum tank, forms self-loopa between delivery pump and homogenizer, opens the 7th valve and drains homogenizing tank tail washings, carry out fast processing to homogenizing tank;
6) disconnect self-loopa, make fat milk in colostrum tank pump into homogenizing tank through delivery pump and homogenizer;
7) in homogenizing tank, the branch road of fat milk band the 10th valve enters outside subsequent technique.
6. fat milk tail washings processing method as claimed in claim 1, is characterized in that: also comprise at least one order 2 step between described 5th step and the 6th step to the 5th step.
7. fat milk tail washings processing method as claimed in claim 1, it is characterized in that: described default tail washings amount is that in colostrum tank, fat milk pumps into through delivery pump and homogenizer the minimum tail washings amount that homogenizer in homogenizing tank process does not enter gas, and described predetermined limit amount is the 4th, the total flow of 5 valves meets the minimum tail washings amount that homogenizer does not enter gas.
8. fat milk tail washings processing method as claimed in claim 7, is characterized in that: described default tail washings amount is 20 kilograms, and described predetermined limit amount is 1 kilogram.
9. fat milk tail washings processing method as claimed in claim 1, is characterized in that: described default aperture is under the maximum prerequisite of satisfied 4th valve flow, the 4th, the total flow of 5 valves meets the maximum opening that homogenizer does not enter gas.
10. fat milk tail washings processing method as claimed in claim 1, is characterized in that: it is that to preset aperture be 33% to the 16%, 5th valve that described 4th valve presets aperture.
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| CN114948871A (en) * | 2022-06-14 | 2022-08-30 | 四川科伦药业股份有限公司 | Fat emulsion injection and preparation method and device thereof |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106074672A (en) * | 2016-07-18 | 2016-11-09 | 四川科伦药业股份有限公司 | Constant temperature system for improving quality of fat milk product |
| CN106074672B (en) * | 2016-07-18 | 2021-10-29 | 四川科伦药业股份有限公司 | Constant temperature system for improving quality of fat milk product |
| CN114948871A (en) * | 2022-06-14 | 2022-08-30 | 四川科伦药业股份有限公司 | Fat emulsion injection and preparation method and device thereof |
| CN114948871B (en) * | 2022-06-14 | 2023-11-17 | 四川科伦药业股份有限公司 | Fat emulsion injection and preparation method and device thereof |
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