CN105434504B - Fat emulsion tail liquid treatment device and method - Google Patents
Fat emulsion tail liquid treatment device and method Download PDFInfo
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- CN105434504B CN105434504B CN201410439291.4A CN201410439291A CN105434504B CN 105434504 B CN105434504 B CN 105434504B CN 201410439291 A CN201410439291 A CN 201410439291A CN 105434504 B CN105434504 B CN 105434504B
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Abstract
The invention discloses a fat emulsion tail liquid treatment device and a method thereof, belonging to the field of fat emulsion preparation. The method for treating the tail liquid sequentially comprises the following steps: self-circulation is formed among the primary emulsion tank, the delivery pump and the homogenizer; pumping the fat emulsion in the primary emulsion tank into a homogenizing tank through a delivery pump and a homogenizer; pumping the fat emulsion in the homogenizing tank into a primary emulsion tank through a delivery pump and a homogenizer; pumping the fat emulsion in the primary emulsion tank into a homogenizing tank through a delivery pump and a homogenizer; the fat milk in the homogenizing tank enters an external subsequent process. The invention relates to a fat emulsion tail liquid treatment device and a method thereof, which can greatly reduce tail liquid discharge on the premise of ensuring safety and reliability.
Description
Technical Field
The invention belongs to the field of fat milk preparation.
Background
Fat emulsion is a homogeneous and stable fat emulsion consisting of refined soybean oil and refined lecithin, and its therapeutic importance is to provide high energy and essential fatty acids under parenteral feeding. The fat which is absorbed by human body from the stomach and intestine is proved to be absorbed by physiology and nutrition to form chylomicron, and the product has the shape and the composition which are extremely similar to those of chylomicron, and can be directly infused into the vein of a patient who cannot eat food to provide fat nutrition.
The fat emulsion tail liquid treatment process is an important basis for ensuring the product quality, ensuring the normal operation of homogenizer equipment and reducing the production cost, and the domestic current fat emulsion tail liquid treatment process is as follows:
1. the fat emulsion tail liquid is completely discharged and is not recovered. The advantages are that: the product quality is ensured; the disadvantages are as follows: the loss is large, the medicine is homogenized for 6 times according to each batch, 20 kg of medicine is discharged each time, 10 batches are produced in one day, and the loss is large in one day: 20 × 6 × 10 — 1200 kg, bottled in 250ML, lost: 4800 bottles, at a cost price of 10 dollars per bottle, lost one month: 4800 × 10 × 30 ═ 1440000 yuan.
2. And finally, homogenizing the liquid medicine recovered from the storage tank according to a production process, and finally, independently filling. 10 batches are produced every day, each batch is homogenized for 6 times, 20 kg of tail liquid is produced each time, and the tail liquid is recovered together in one day: 20 × 6 × 10 ═ 1200 kg. However, concentrated discharge of the tailings into a storage tank is extremely difficult to operate in the production process, product quality is difficult to guarantee, and the tailings are mixed together in batches and stored for too long, so that the product has great quality risk.
Disclosure of Invention
The invention aims to: provides a fat emulsion tail liquid treatment device and a method thereof which can greatly reduce tail liquid discharge amount on the premise of ensuring safety.
The purpose of the invention is realized by the following technical scheme:
a fat emulsion tail liquid treatment system comprises a colostrum tank, a homogenizing tank, a delivery pump and a homogenizer, wherein the colostrum tank, the homogenizing tank, the delivery pump and the homogenizer form a circulating system through a pipeline and valves on the pipeline, the delivery pump is connected with the homogenizer in series and further connected with the colostrum tank and the homogenizing tank in series, the outlet ends of the colostrum tank and the homogenizing tank are communicated with the inlet end of the delivery pump, the outlet end of the homogenizer is respectively communicated with the inlet ends of the colostrum tank and the homogenizing tank, a branch with a 10 th valve is further arranged on the pipeline between the outlet end of the delivery pump and the inlet end of the homogenizing tank and communicated with the outside, a branch with a 2 nd valve and a branch with a 7 th valve are further respectively arranged at the outlet ends of the colostrum tank and the homogenizing tank and communicated with the outside, 12 th valve and a 9 th valve are respectively arranged at the inlet ends of the colostrum tank and the homogenizing tank, and a 4 th valve is respectively arranged on the pipeline between the outlet ends of the colostrum tank and the inlet end of the delivery pump, 5 valves, still all be equipped with tail liquid volume monitoring device in colostrum jar and the homogeneity jar, and the 4 th valve with the tail liquid monitoring device electricity of homogeneity jar is connected and can be according to its tail liquid volume signal control aperture that gives, the 5 th valve with the tail liquid monitoring device electricity of colostrum jar is connected and can be according to its tail liquid volume signal control aperture that gives.
Optionally, the outlet end of the colostrum tank is provided with a 1 st valve, and the outlet end of the homogenizing tank is provided with a 8 th valve.
As a further option, a 3 rd valve is further arranged on a pipeline between the 1 st valve and the 4 th valve, and the 1 st valve, the 2 nd valve and the 3 rd valve are communicated through a tee joint; and a 6 th valve is also arranged on a pipeline between the 8 th valve and the 5 th valve, and the 6 th, 7 th and 8 th valves are communicated by a tee joint.
Optionally, a 11 th valve is further arranged on a pipeline between the 12 th valve and the 9 th valve, the 11 th valve and the 12 th valve are communicated with the homogenizer through a tee joint, and the 9 th valve, the 10 th valve and the 11 th valve are communicated through a tee joint.
A method for treating tail liquid by adopting the fat emulsion tail liquid treatment system sequentially comprises the following steps:
1) self-circulation is formed among the primary emulsion tank, the delivery pump and the homogenizer;
2) cutting off self-circulation, pumping the fat milk in the primary emulsion tank into a homogenizing tank through a delivery pump and a homogenizer, automatically adjusting the 4 th valve and the 5 th valve to a preset opening degree when the fat milk in the primary emulsion tank is reduced to a preset tail liquid amount, and simultaneously pumping the fat milk from the primary emulsion tank and the homogenizing tank into the homogenizing tank through the delivery pump and the homogenizer;
3) when the tail liquid in the colostrum tank is reduced to a preset limit amount, the 4 th valve is closed, the 5 th valve is fully opened to form self circulation among the homogenizing tank, the delivery pump and the homogenizer, the 2 nd valve is opened to drain the tail liquid in the colostrum tank, and the colostrum tank is quickly treated;
4) closing the 2 nd valve, cutting off self-circulation, pumping the fat milk in the homogenizing tank into the primary emulsion tank through the delivery pump and the homogenizer, automatically adjusting the 4 th and 5 th valves to opposite preset opening degrees when the fat milk in the homogenizing tank is reduced to the preset tail liquid amount, and simultaneously pumping the fat milk from the primary emulsion tank and the homogenizing tank into the primary emulsion tank through the delivery pump and the homogenizer;
5) when the tail liquid in the homogenizing tank is reduced to the preset limit amount, closing the 5 th valve, fully opening the 4 th valve to enable self circulation to be formed among the primary emulsion tank, the delivery pump and the homogenizer, opening the 7 th valve to drain the tail liquid in the homogenizing tank, and quickly processing the homogenizing tank;
6) cutting off self-circulation to pump the fat emulsion in the primary emulsion tank into the homogenizing tank through the delivery pump and the homogenizer;
7) the fat milk in the homogenizing tank enters the external subsequent process through a branch with a 10 th valve.
In the scheme, no matter the emulsion is of different varieties and specifications, the emulsion can be homogenized for many times, so that the continuous production can ensure stable pressure, good emulsion quality and high efficiency.
Optionally, at least one step 2 to step 5 is included between the step 5 and the step 6.
In the scheme, according to the requirements of the content of the refined lecithin in the fat milk, the production quality and the like, repeated reciprocating can be further carried out for many times.
Optionally, the preset tail liquid amount is the lowest tail liquid amount of the homogenizer which does not enter gas in the process that the fat emulsion in the primary emulsion tank is pumped into the homogenizing tank through the delivery pump and the homogenizer, and the preset limit amount is the lowest tail liquid amount of the homogenizer which does not enter gas and is satisfied by the total flow of the 4 th valve and the 5 th valve.
In the above scheme, in order to ensure safe and reliable production and meet the flow requirement of the homogenizer, the lowest tail liquid amount without gas entrainment is limited when all the tail liquid enters the homogenizer through the 4 th valve and simultaneously through the 4 th and 5 th valves.
As a further option, the preset tail liquid amount is 20 kg, and the preset limit amount is 1 kg.
Alternatively, on the premise that the preset opening degree meets the requirement that the flow of the 4 th valve is maximum, the total flow of the 4 th and 5 th valves meets the maximum opening degree that the homogenizer does not enter gas.
According to the scheme, when the flow of the 4 th valve is maximum, backflow from the homogenizing tank to the primary emulsion tank can be avoided, tail liquid in the primary emulsion tank can be extracted as soon as possible, and the efficiency is improved; the total flow of the 4 th valve and the 5 th valve meets the maximum opening degree of the homogenizer without entering gas, thereby not only ensuring the flow requirement of safe and reliable operation of the homogenizer, but also meeting the highest operation efficiency. On the contrary, the preset opening degree means that the preset opening degrees of the 4 th valve and the 5 th valve are exchanged, that is, the preset opening degree of the 4 th valve is adjusted to the original preset opening degree of the 5 th valve, and similarly, the preset opening degree of the 5 th valve is adjusted to the original preset opening degree of the 4 th valve.
As a further option, the preset opening degree of the 4 th valve is 16%, and the preset opening degree of the 5 th valve is 33%.
The aforementioned main solutions of the present invention and their respective further alternatives can be freely combined to form a plurality of solutions, all of which are solutions that can be adopted and claimed by the present invention: according to the present invention, each option can be combined with other options at will, and those skilled in the art can understand that various combinations are all the technical schemes to be protected by the present invention according to the prior art and the common general knowledge after understanding the scheme of the present invention, and the technical schemes are not exhaustive herein.
The invention has the beneficial effects that:
1. safe and reliable, stopped the quality risk that the fat emulsion tail liquid exists in the transportation.
2. The volume of the fat emulsion tail liquid is reduced, the final volume of the fat emulsion tail liquid discharged by using the method can reach 1 kg at least, so that the production cost is greatly reduced, the medicine is homogenized for 6 times according to each batch, 1 kg is discharged each time, 10 batches are produced in one day, and the loss is caused in one day: 1 × 6 × 10 × 60 kg, bottled in 250ML, lost: 120 bottles, at a cost price of 10 dollars per bottle, lost one month: 120 x 10 x 30 ═ 36000 yuan. Compared with the process for treating the fat emulsion tail liquid by centralized discharge, the process has the advantages that: 1440000-36000 ═ 1304000 yuan.
Drawings
FIG. 1 is a schematic flow diagram of an apparatus according to an embodiment of the present invention;
wherein 1 is a primary emulsion tank, 2 is a homogenizing tank, 3 is a homogenizer, and 4 is a delivery pump.
Detailed Description
The following non-limiting examples serve to illustrate the invention.
As shown in figure 1, a fat emulsion tail liquid treatment system comprises a colostrum tank 1, a homogenization tank 2, a delivery pump 4 and a homogenizer 3, wherein the colostrum tank 1, the homogenization tank 2, the delivery pump 4 and the homogenizer 3 form a circulating system by being communicated through a pipeline and valves thereon, the delivery pump 4 is connected in series with the homogenizer 3 and further connected in series with the colostrum tank 1 and the homogenization tank 2 which are connected in parallel, outlet ends of the colostrum tank 1 and the homogenization tank 2 are communicated with an inlet end of the delivery pump 4, an outlet end of the homogenizer 3 is respectively communicated with inlet ends of the colostrum tank 1 and the homogenization tank 2, a branch with a 10 th valve is further arranged on the pipeline between the outlet end of the delivery pump 4 and the inlet end of the homogenization tank 2 and communicated with the outside, branch circuits with valves 2 and 7 th valves are further respectively arranged at the outlet ends of the colostrum tank 1 and the homogenization tank 2 and communicated with the outside, and a 12 th branch circuit is respectively arranged at the inlet ends of the colostrum tank 1 and the homogenization tank 2, 9 valves, be equipped with the 4 th on the pipeline between the exit end of colostrum jar 1 and homogeneity jar 2 and the entry end of delivery pump 4 respectively, 5 valves, still all be equipped with tail liquid volume monitoring device in colostrum jar 1 and the homogeneity jar 2, and the 4 th valve is connected with the tail liquid monitoring device electricity of homogeneity jar 2 and can be according to its tail liquid volume signal control aperture that gives, and the 5 th valve is connected with the tail liquid monitoring device electricity of colostrum jar 1 and can be according to its tail liquid volume signal control aperture that gives. Alternatively, as shown in this embodiment, the outlet end of the colostrum tank 1 is provided with the 1 st valve, and the outlet end of the homogenization tank 2 is provided with the 8 th valve. A 3 rd valve is also arranged on a pipeline between the 1 st valve and the 4 th valve, and the 1 st, the 2 nd and the 3 rd valves are communicated by a tee joint; a 6 th valve is also arranged on a pipeline between the 8 th valve and the 5 th valve, and the 6 th, 7 th and 8 th valves are communicated by a tee joint. The pipeline between the 12 th valve and the 9 th valve is also provided with an 11 th valve, the 11 th valve and the 12 th valve are communicated with the homogenizer 3 by a tee joint, and the 9 th valve, the 10 th valve and the 11 th valve are communicated by a tee joint.
A method for treating tail liquid by adopting the fat emulsion tail liquid treatment system sequentially comprises the following steps:
1) self-circulation is formed among the primary emulsion tank 1, the delivery pump 4 and the homogenizer 3;
2) the self-circulation is cut off, so that the fat milk in the primary milk tank 1 is pumped into the homogenizing tank 2 through the delivery pump 4 and the homogenizer 3, and the 4 th and 5 th valves are automatically adjusted to a preset opening degree when the fat milk in the primary milk tank 1 is reduced to a preset tail liquid amount, and meanwhile, the fat milk is pumped from the primary milk tank 1 and the homogenizing tank 2 and is pumped into the homogenizing tank 2 through the delivery pump 4 and the homogenizer 3;
3) when the tail liquid in the colostrum tank 1 is reduced to a preset limit amount, the 4 th valve is closed, the 5 th valve is opened fully to form self circulation among the homogenizing tank 2, the delivery pump 4 and the homogenizer 3, the 2 nd valve is opened to drain the tail liquid in the colostrum tank 1, and the colostrum tank 1 is treated quickly;
4) closing the 2 nd valve, cutting off self-circulation, pumping the fat milk in the homogenizing tank 2 into the primary emulsion tank 1 through the delivery pump 4 and the homogenizer 3, automatically adjusting the 4 th and 5 th valves to opposite preset opening degrees when the fat milk in the homogenizing tank 2 is reduced to a preset tail liquid amount, and simultaneously pumping the fat milk from the primary emulsion tank 1 and the homogenizing tank 2 into the primary emulsion tank 1 through the delivery pump 4 and the homogenizer 3;
5) when the tail liquid in the homogenizing tank 2 is reduced to a preset limit amount, the 5 th valve is closed, the 4 th valve is fully opened to form self circulation among the primary emulsion tank 1, the delivery pump 4 and the homogenizing machine 3, the 7 th valve is opened to drain the tail liquid in the homogenizing tank 2, and the homogenizing tank 2 is rapidly treated;
6) the self-circulation is cut off, so that the fat milk in the primary milk tank 1 is pumped into the homogenizing tank 2 through the delivery pump 4 and the homogenizer 3;
7) the fat emulsion in the homogenizing tank 2 enters external subsequent processes, such as a finished product filling process, through a branch with a 10 th valve.
Optionally, the preset tail liquid amount is the lowest tail liquid amount of the homogenizer 3 which does not enter gas in the process that the fat emulsion in the primary emulsion tank 1 is pumped into the homogenizing tank 2 through the delivery pump 4 and the homogenizer 3, and the preset limit amount is the lowest tail liquid amount of the homogenizer 3 which does not enter gas and is satisfied by the total flow of the 4 th valve and the 5 th valve. As shown in this example, the predetermined amount of tail gas is 20 kg, and the predetermined limit amount is 1 kg. On the premise that the preset opening degree meets the requirement that the flow of the 4 th valve is maximum, the total flow of the 4 th valve and the 5 th valve meets the maximum opening degree that the homogenizer 3 does not enter gas. In this embodiment, the preset opening of the 4 th valve is 16%, and the preset opening of the 5 th valve is 33%.
According to the requirements of the content of the refined lecithin in the fat milk, the production quality and the like, the method can further repeat for a plurality of times: and at least one process operation from the 2 nd step to the 5 th step is carried out between the 5 th step and the 6 th step.
Taking the system shown in fig. 1 as an example, a specific operation example is as follows:
carry out the homogeneity to 1 fat breast in colostrum jar, at first open 1 st, 3, 4, 12 valves, open delivery pump 4, isotropic symmetry 3, make fat breast through delivery pump 4, isotropic symmetry 3, pipeline form from the circulation system, restart to carry out the pressure regulating to isotropic symmetry 3, open 11 th, 9 th valve simultaneously, close 12 th valve, the reduction of 1 tail fluid weight in 1 tail fluid volume monitoring device automatic monitoring colostrum jar, when 20 kilograms of tail fluid volume are predetermine to 1 surplus only in colostrum jar at first, just be fat emulsion tail fluid. At the moment, the 5 th valve is automatically adjusted to the preset opening degree of 33%, the 4 th valve is automatically adjusted to the preset opening degree of 16%, and the 8 th valve and the 6 th valve are opened. When the weight of tail liquid in the primary emulsion tank 1 reaches 1 kilogram of the preset limit quantity, the 5 th valve is opened, and the 3 rd valve and the 4 th valve are closed simultaneously. Open 2 nd valve row to the greatest extent colostrum jar 1 and the tail liquid in the pipeline, carry out rapid processing to colostrum jar 1, close 1 st after finishing, 2 nd valve, open 12 th valve, close 11 th, 9 th valve, make the fat emulsion of homogeneity jar 2 shift to colostrum jar 1, the reduction of 2 tail liquid weight of homogeneity jar of 2 tail liquid monitoring devices automatic monitoring homogeneity jar, when the fat emulsion of homogeneity jar 2 reduces to predetermineeing tail liquid volume 20 kilograms, just be fat emulsion tail liquid, 4 th valve automatically regulated is to predetermineeing aperture 33%, 5 th valve automatically regulated is to predetermineeing aperture 16%. And opening the 1 st valve and the 3 rd valve, and when the weight of the tail liquid in the homogenizing tank 2 is 1 kg of the preset limit quantity, fully opening the 4 th valve and simultaneously closing the 6 th valve and the 5 th valve. Opening 7 th valve to drain the tail liquid in homogenizing tank 2 and its pipeline, quickly treating homogenizing tank 2, closing 8 th and 7 th valves, opening 11 th and 9 th valves, and closing 12 th valve to transfer the fat emulsion in the primary emulsion tank 1 to homogenizing tank 2. Finally, the fat milk in the homogenizing tank 2 enters an external finished product filling procedure through a branch with a 10 th valve.
The above description is only for the purpose of illustrating the preferred embodiments of the present invention and is not to be construed as limiting the invention, and any modifications, equivalents and improvements made within the spirit and principle of the present invention are intended to be included within the scope of the present invention.
Claims (10)
1. A fat emulsion tail liquid treatment system is characterized by comprising a colostrum tank, a homogenizing tank, a conveying pump and a homogenizer, wherein the colostrum tank, the homogenizing tank, the conveying pump and the homogenizer are communicated through a pipeline and valves on the pipeline to form a circulating system, the conveying pump is connected with the homogenizer in series and is further connected with the colostrum tank and the homogenizing tank which are connected in parallel in series, outlet ends of the colostrum tank and the homogenizing tank are communicated with an inlet end of the conveying pump, an outlet end of the homogenizer is communicated with inlet ends of the colostrum tank and the homogenizing tank respectively, a branch with a 10 th valve is further arranged on the pipeline between the outlet end of the conveying pump and the inlet end of the homogenizing tank and is communicated with the outside, branch circuits with 2 nd and 7 th valves are further arranged at outlet ends of the colostrum tank and the homogenizing tank and are communicated with the outside respectively, 12 th and 9 th valves are arranged at inlet ends of the colostrum tank and the homogenizing tank, and the pipeline between the outlet ends of the conveying pump are provided with a 4 th valve, a pump and a pump respectively, 5 valves, still all be equipped with tail liquid volume monitoring device in colostrum jar and the homogeneity jar, and the 4 th valve with the tail liquid monitoring device electricity of homogeneity jar is connected and can be according to its tail liquid volume signal control aperture that gives, the 5 th valve with the tail liquid monitoring device electricity of colostrum jar is connected and can be according to its tail liquid volume signal control aperture that gives.
2. The fat emulsion tail treatment system of claim 1, wherein: the exit end of colostrum jar is equipped with 1 st valve, the exit end of homogeneity jar is equipped with 8 th valve.
3. The fat emulsion tail treatment system of claim 2, wherein: a 3 rd valve is also arranged on a pipeline between the 1 st valve and the 4 th valve, and the 1 st, the 2 nd and the 3 rd valves are communicated by a tee joint; and a 6 th valve is also arranged on a pipeline between the 8 th valve and the 5 th valve, and the 6 th, 7 th and 8 th valves are communicated by a tee joint.
4. The fat emulsion tail treatment system of claim 1, wherein: and a 11 th valve is also arranged on a pipeline between the 12 th valve and the 9 th valve, the 11 th valve and the 12 th valve are communicated with the homogenizer by a tee joint, and the 9 th valve, the 10 th valve and the 11 th valve are communicated by a tee joint.
5. A method for treating tail liquid by using the fat emulsion tail liquid treatment system as claimed in any one of claims 1 to 4, which is characterized by comprising the following steps in sequence:
1) self-circulation is formed among the primary emulsion tank, the delivery pump and the homogenizer;
2) cutting off self-circulation, pumping the fat milk in the primary emulsion tank into a homogenizing tank through a delivery pump and a homogenizer, automatically adjusting the 4 th valve and the 5 th valve to a preset opening degree when the fat milk in the primary emulsion tank is reduced to a preset tail liquid amount, and simultaneously pumping the fat milk from the primary emulsion tank and the homogenizing tank into the homogenizing tank through the delivery pump and the homogenizer;
3) when the tail liquid in the colostrum tank is reduced to a preset limit amount, the 4 th valve is closed, the 5 th valve is fully opened to form self circulation among the homogenizing tank, the delivery pump and the homogenizer, the 2 nd valve is opened to drain the tail liquid in the colostrum tank, and the colostrum tank is quickly treated;
4) closing the 2 nd valve, cutting off self-circulation, pumping the fat milk in the homogenizing tank into the primary emulsion tank through the delivery pump and the homogenizer, automatically adjusting the 4 th and 5 th valves to opposite preset opening degrees when the fat milk in the homogenizing tank is reduced to the preset tail liquid amount, and simultaneously pumping the fat milk from the primary emulsion tank and the homogenizing tank into the primary emulsion tank through the delivery pump and the homogenizer;
5) when the tail liquid in the homogenizing tank is reduced to the preset limit amount, closing the 5 th valve, fully opening the 4 th valve to enable self circulation to be formed among the primary emulsion tank, the delivery pump and the homogenizer, opening the 7 th valve to drain the tail liquid in the homogenizing tank, and quickly processing the homogenizing tank;
6) cutting off self-circulation to pump the fat emulsion in the primary emulsion tank into the homogenizing tank through the delivery pump and the homogenizer;
7) the fat milk in the homogenizing tank enters the external subsequent process through a branch with a 10 th valve.
6. The fat emulsion tail liquid treatment method according to claim 1, characterized in that: and at least one step from 2 to 5 is also included between the step 5 and the step 6.
7. The fat emulsion tail liquid treatment method according to claim 1, characterized in that: the preset tail liquid amount is the lowest tail liquid amount of the homogenizer which does not enter gas in the process that the fat emulsion in the primary emulsion tank is pumped into the homogenizing tank through the delivery pump and the homogenizer, and the preset limit amount is the lowest tail liquid amount of the homogenizer which does not enter gas and is satisfied by the total flow of the 4 th valve and the 5 th valve.
8. The fat emulsion tail liquid treatment method according to claim 7, characterized in that: the preset tail liquid amount is 20 kg, and the preset limit amount is 1 kg.
9. The fat emulsion tail liquid treatment method according to claim 1, characterized in that: on the premise that the preset opening degree meets the requirement that the flow of the 4 th valve is maximum, the total flow of the 4 th valve and the 5 th valve meets the maximum opening degree that the homogenizer does not enter gas.
10. The fat emulsion tail liquid treatment method according to claim 1, characterized in that: the preset opening degree of the 4 th valve is 16%, and the preset opening degree of the 5 th valve is 33%.
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| 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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| WO2001068059A1 (en) * | 2000-03-15 | 2001-09-20 | Instituto Cientifico Y Tecnologico De Navarra, S.A. | Method and device for the production of microparticles for controlled release of water-soluble pharmaceuticals and viral vectors. application to the administration of plasmid dna and defective recombinant adenovirus |
| CN103381195A (en) * | 2012-05-02 | 2013-11-06 | 四川科伦药业股份有限公司 | Fat emulsion injection and preparation method thereof |
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| DE19942283A1 (en) * | 1999-09-04 | 2001-03-15 | Messer Griesheim Gmbh | Apparatus for producing stable, concentrated liquid preparation containing gaseous or volatile anesthetic, e.g. xenon, including premixing and fine mixing or homogenization stages |
| CN1186011C (en) * | 2002-09-17 | 2005-01-26 | 西安力邦医药科技有限责任公司 | automatic liposome preparation apparatus and method for prepaving liplsome by same |
| CN101143210A (en) * | 2006-09-13 | 2008-03-19 | 乌鲁木齐远新食疗有限公司 | Compound fatty milk oral preparation |
| CN201350218Y (en) * | 2008-12-03 | 2009-11-25 | 天津天士力制药股份有限公司 | Dripping pill production line |
| CN201930254U (en) * | 2010-12-24 | 2011-08-17 | 浙江威仕生物科技有限公司 | Double-embedding microcapsule production equipment |
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| CN203196585U (en) * | 2013-03-20 | 2013-09-18 | 南京高正农用化工有限公司 | Suspending agent production line |
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| CN204050374U (en) * | 2014-08-29 | 2014-12-31 | 四川科伦药业股份有限公司 | A kind of fat milk tail washings blood processor |
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| CN103381195A (en) * | 2012-05-02 | 2013-11-06 | 四川科伦药业股份有限公司 | Fat emulsion injection and preparation method thereof |
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