CN204050374U - A kind of fat milk tail washings blood processor - Google Patents
A kind of fat milk tail washings blood processor Download PDFInfo
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- CN204050374U CN204050374U CN201420496098.XU CN201420496098U CN204050374U CN 204050374 U CN204050374 U CN 204050374U CN 201420496098 U CN201420496098 U CN 201420496098U CN 204050374 U CN204050374 U CN 204050374U
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- tank
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- tail washings
- colostrum
- homogenizing
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Abstract
The utility model discloses a kind of fat milk tail washings blood processor, belong to fat milk preparation field, processing system comprises 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.This utility model is under the safe and reliable prerequisite of a kind of guarantee, significantly reduces the fat milk tail washings blood processor of tail liquid emissions amount.
Description
Technical field
This utility model 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.
Utility model content
The purpose of this utility model is: under proposing the safe and reliable prerequisite of a kind of guarantee, significantly reduce the fat milk tail washings blood processor of tail liquid emissions amount.
This utility model object 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.
As selection, 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, the 5th valve is electrically connected the tail washings amount signal that also can provide according to it and controls aperture with the tail washings supervising device of described colostrum tank.
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.
Workflow of the present utility model:
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.
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 comprise at least one order 2 step between described 5th step and the 6th step to the 5th step.
In order to ensure producing safely and reliably, meet the traffic requirement of homogenizer, limit all via the 4th valve, and the minimum tail washings amount of not bringing gas into simultaneously via the 4th, when 5 valves enter homogenizer: 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.As selection, described default tail washings amount is 20 kilograms, and described predetermined limit amount is 1 kilogram.
Further, 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.Thus, 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 selection, it is that to preset aperture be 33% to the 16%, 5th valve that described 4th valve presets aperture.
No matter take this utility model device, be different cultivars, specification Emulsion, can by homogenizing process repeatedly, and continuous seepage can ensure that pressure stability, Emulsion quality are good, efficiency is high thus.
Aforementioned this utility model main formula case and each further selection scheme thereof can independent assortment to form multiple scheme; be this utility model can adopt and claimed scheme: as this utility model; 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 this utility model scheme; be the claimed technical scheme of this utility model, do not do exhaustive at this.
The beneficial effects of the utility model:
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 this utility model 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 this utility model embodiment;
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 this utility model.
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.
The workflow of aforementioned fat milk tail washings processing system, 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 utility model; not in order to limit this utility model; all do within spirit of the present utility model and principle any amendment, equivalent to replace and improvement etc., all should be included within protection domain of the present utility model.
Claims (5)
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.
2. fat milk tail washings processing system as claimed in claim 1, it is characterized in that: 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, the 5th valve is electrically connected the tail washings amount signal that also can provide according to it and controls aperture with the tail washings supervising device of described colostrum tank.
3. 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.
4. fat milk tail washings processing system as claimed in claim 3, 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.
5. 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.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420496098.XU CN204050374U (en) | 2014-08-29 | 2014-08-29 | A kind of fat milk tail washings blood processor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420496098.XU CN204050374U (en) | 2014-08-29 | 2014-08-29 | A kind of fat milk tail washings blood processor |
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| Publication Number | Publication Date |
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| CN204050374U true CN204050374U (en) | 2014-12-31 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201420496098.XU Withdrawn - After Issue CN204050374U (en) | 2014-08-29 | 2014-08-29 | A kind of fat milk tail washings blood processor |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104825392A (en) * | 2015-04-24 | 2015-08-12 | 四川科伦药业股份有限公司 | Treatment system for reducing fat emulsion peroxide value and methoxyaniline value and method thereof |
| CN105434504A (en) * | 2014-08-29 | 2016-03-30 | 四川科伦药业股份有限公司 | Fat emulsion tail liquid treatment apparatus and method thereof |
| CN109569300A (en) * | 2018-12-14 | 2019-04-05 | 上海景峰制药有限公司 | A kind of system and method for separation of fermentative broth purifying |
-
2014
- 2014-08-29 CN CN201420496098.XU patent/CN204050374U/en not_active Withdrawn - After Issue
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105434504A (en) * | 2014-08-29 | 2016-03-30 | 四川科伦药业股份有限公司 | Fat emulsion tail liquid treatment apparatus and method thereof |
| CN104825392A (en) * | 2015-04-24 | 2015-08-12 | 四川科伦药业股份有限公司 | Treatment system for reducing fat emulsion peroxide value and methoxyaniline value and method thereof |
| CN104825392B (en) * | 2015-04-24 | 2018-03-20 | 四川科伦药业股份有限公司 | Reduce Fat Emulsion peroxide value and anisidine value processing system and its method |
| CN109569300A (en) * | 2018-12-14 | 2019-04-05 | 上海景峰制药有限公司 | A kind of system and method for separation of fermentative broth purifying |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20210918 Address after: 152000 Dongcheng District, Qing'an County, Suihua City, Heilongjiang Province Patentee after: HEILONGJIANG KELUN PHARMACEUTICAL Co.,Ltd. Address before: 610500 south two road, Satellite City Industrial Development Zone, Xindu District, Chengdu, Sichuan Patentee before: Sichuan Kelun Pharmaceutical Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20141231 Effective date of abandoning: 20211015 |
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| AV01 | Patent right actively abandoned |
Granted publication date: 20141231 Effective date of abandoning: 20211015 |
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| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |