CN202089859U - Heparin sodium waste liquid treatment equipment - Google Patents
Heparin sodium waste liquid treatment equipment Download PDFInfo
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- CN202089859U CN202089859U CN2011201865462U CN201120186546U CN202089859U CN 202089859 U CN202089859 U CN 202089859U CN 2011201865462 U CN2011201865462 U CN 2011201865462U CN 201120186546 U CN201120186546 U CN 201120186546U CN 202089859 U CN202089859 U CN 202089859U
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- heparin sodium
- sodium waste
- container
- treatment equipment
- outer cavity
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Abstract
The utility model discloses heparin sodium waste liquid treatment equipment which can be used for preparing protein feed, and comprises an initial vapor generation container for vaporizing concentrated heparin sodium waste liquid, wherein the initial vapor generation container is provided with a sealed isolation inner housing and an outer cavity housing, the sealed isolation inner housing is fixedly arranged in the outer cavity housing, the interior of the sealed isolation inner housing is a heating inner housing, a liquid containing outer cavity is formed between the sealed isolation inner housing and the outer cavity housing, a heating device is arranged in the heating inner cavity, the heparin sodium waste liquid is contained in the liquid containing outer cavity, the outer cavity housing is provided with a vapor outlet and a liquid inlet, and the bottom of the outer cavity housing is provided with a concentrated liquid discharge outlet. With the heparin sodium waste liquid treatment equipment disclosed by the utility model, the heating efficiency of the heparin sodium waste liquid can be improved, the energy consumption can be reduced, and simultaneously, when the heparin sodium waste liquid is treated by adopting the equipment, the pollution to the environment can be avoided, and the protein feed can be obtained.
Description
Technical field
The utility model discloses a kind of waste liquor treatment equipment, be specifically related to a kind of heparin sodium waste liquor treatment equipment.
Background technology
At present, heparin sodium is the main valuable drug as the treatment cardiovascular and cerebrovascular in the world, contains a large amount of nitrogen things in its waste water after extracting heparin sodium, as for a long time without processing and directly discharging contact easy formation nitrous acid with air, thereby the formation carcinogen.Existing heparin sodium manufacturing enterprise all is that the heparin sodium waste liquid directly is discharged in the river in the process of producing heparin sodium, has formed havoc and pollution to environment.
The utility model content
Technical problem to be solved in the utility model provides a kind ofly carries out evaporation concentration to the heparin sodium waste liquid and obtains the heparin sodium waste liquor treatment equipment of protein fodder.
The technical scheme that its technical problem that solves the utility model adopts is: the heparin sodium waste liquor treatment equipment, comprise the initial steam generation container that is used for evaporation concentration heparin sodium waste liquid, described initial steam generation container has seal isolation inner casing and outer cavity shell, the seal isolation inner casing is fixedly installed in the outer cavity shell, in the seal isolation inner casing is heating bore, be Sheng liquid exocoel between seal isolation inner casing and the outer cavity shell, in heating bore, be provided with heating unit, the heparin sodium waste liquid is contained in the liquid exocoel, outer cavity shell is provided with vapour outlet and liquid-inlet, and the exocoel housing bottom is provided with the concentrated solution discharge outlet.
Further be to be negative pressure in the described Sheng liquid exocoel.
Further be, in heating bore, be provided with two ends and be fixedly connected on heat transfer tube on the seal isolation inner casing, and the two ends of heat transfer tube all with contain the liquid exocoel and communicate.
Further be, cavity shell is provided with the fume emission mouth outside, the seal isolation inner casing is provided with the smoke exhaust pipe that is communicated with fume emission mouth and heating bore, and the end sealing of described smoke exhaust pipe is arranged on fume emission mouth place, and the other end sealing is arranged on the seal isolation inner casing.
Further be that described smoke exhaust pipe is the coiling shape.
Further be that the vapour outlet of described initial steam generation container is connected in series with a plurality of container for evaporation by pipeline.
Further be, the inner chamber of described a plurality of container for evaporation is negative pressure, and the internal pressure of first container for evaporation that the vapour outlet of initial steam generation container connects is less than the pressure of containing the liquid exocoel in the initial steam generation container; And on the flow direction of steam, the chamber pressure of container for evaporation that is positioned at the place ahead is greater than the chamber pressure of the container for evaporation that is positioned at the rear.
The beneficial effects of the utility model are: because heparin sodium waste liquor treatment equipment of the present utility model both had been provided with heating bore, be provided with again and contain the liquid exocoel, like this, the heparin sodium waste liquid is being heated when concentrating, heat diffuses to its periphery from heating bore and contains in the heparin sodium waste liquid of splendid attire the liquid exocoel, heat can fully be absorbed by the heparin sodium waste liquid, thereby has improved the heating efficiency to the heparin sodium waste liquid, also just can reduce the consumption of the energy; In addition, adopt this equipment that the heparin sodium waste liquid is handled, can also effectively avoid the heparin sodium waste liquid that environment is done great damage and pollute, and can prepare protein fodder, be particluarly suitable for producing in the enterprise of heparin sodium and apply.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
Be labeled as among the figure: heating unit 1, heating bore 2, Sheng liquid exocoel 3, seal isolation inner casing 4, outer cavity shell 5, vapour outlet 6, liquid-inlet 7, concentrated solution discharge outlet 8, heat transfer tube 9, smoke exhaust pipe 10, container for evaporation 11, fume emission mouth 12.
Embodiment
Below in conjunction with drawings and Examples the utility model is further specified.
As shown in Figure 1, heparin sodium waste liquor treatment equipment of the present utility model, comprise the initial steam generation container that is used for evaporation concentration heparin sodium waste liquid, described initial steam generation container has seal isolation inner casing 4 and outer cavity shell 5, seal isolation inner casing 4 is fixedly installed in the outer cavity shell 5, in the seal isolation inner casing 4 is heating bore 2, be Sheng liquid exocoel 3 between seal isolation inner casing 4 and the outer cavity shell 5, in heating bore 2, be provided with heating unit 1, the heparin sodium waste liquid is contained in the liquid exocoel 3, outer cavity shell 5 is provided with vapour outlet 6 and liquid-inlet 7, and outer cavity shell 5 bottoms are provided with concentrated solution discharge outlet 8.Because heparin sodium waste liquor treatment equipment of the present utility model both had been provided with heating bore 2, be provided with again and contain liquid exocoel 3, like this, the heparin sodium waste liquid is being heated when concentrating, heat diffuses to its periphery from heating bore 2 and contains in the heparin sodium waste liquid of splendid attire the liquid exocoel 3, heat can fully be absorbed by the heparin sodium waste liquid, thereby has improved the heating efficiency to the heparin sodium waste liquid, also just can reduce the consumption of the energy.The heparin sodium waste liquid is being heated in the spissated process, and steam is discharged from vapour outlet 6, discharges from concentrated solution discharge outlet 8 and concentrate later heparin sodium concentrated solution, handles through oven dry, just can obtain protein fodder.
On the basis of above-mentioned embodiment,, be negative pressure in the described Sheng liquid exocoel 3 in order further to reduce the consumption of the energy.Generally the heparin sodium waste liquid temperature that obtains after heparin sodium extracts is about 55 ℃, be set to negative pressure by the inside of containing liquid exocoel 3, can reduce the boiling temperature of heparin sodium waste liquid, thereby can make the boiling of heparin sodium waste liquid under 55 ℃ the temperature being a bit larger tham, can reduce the consumption of the energy greatly.As the pressure of containing liquid exocoel 3 is set to-0.09MP, can make the boiling of heparin sodium waste liquid so about 65 ℃.
In order further to improve heating efficiency, in heating bore 2, be provided with two ends and be fixedly connected on heat transfer tube 9 on the seal isolation inner casing 4, and the two ends of heat transfer tube 9 all communicate with Sheng liquid exocoel 3 the heparin sodium waste liquid.Like this, when temperature raises in heating bore 2, except heat being changed to Sheng liquid exocoel 3 by seal isolation inner casing 4, can also heat be changed in the heparin sodium waste liquid to the heat transfer tube 9 by heat transfer tube 9, improved the heat interchanging area of whole heat-processed, thereby can improve heating efficiency the heparin sodium waste liquid.
In the above embodiment, discharge for the ease of flue gas in the heat-processed, cavity shell 5 is provided with fume emission mouth 12 outside, seal isolation inner casing 4 is provided with the smoke exhaust pipe 10 that is communicated with fume emission mouth 12 and heating bore 2, the one end sealing of described smoke exhaust pipe 10 is arranged on fume emission mouth 12 places, and the other end sealing is arranged on the seal isolation inner casing 4.Like this, flue gas can emit by smoke exhaust pipe 10, fume emission mouth 12.
In order to make full use of the heat that produces in the heating bore 2, on the basis of above-mentioned embodiment, described smoke exhaust pipe 10 is the coiling shape.As shown in Figure 1, like this, when flue gas passes through the smoke exhaust pipe 10 of coiling, can fully the heat in the flue gas be changed to the heparin sodium waste liquid of containing liquid exocoel 3, can further reduce the consumption of the energy.
In the above embodiment, the steam that produces in the initial steam generation container can directly be discharged from vapour outlet 6, but obviously, also has a large amount of heat energy in the steam of this discharge, in order to make full use of this heat energy, the vapour outlet 6 of described initial steam generation container is connected in series with a plurality of container for evaporation 11 by pipeline.As adopting the normal triple effect equipment (every effect equipment is a container for evaporation 11) that adopts in the prior art, its first effect equipment is by the vapour outlet 6 of the initial steam generation container of pipe connection, the second effect equipment is then imitated the vapour outlet of equipment by pipe connection first, triple effect equipment is then imitated the vapour outlet of equipment by pipe connection second.Certainly the amount of container for evaporation 11 also can be greater than three, as long as the steam heat that can effectively utilize previous container for evaporation 11 to produce.Container for evaporation 11 has two effects, the first is carried out condensation (certainly to the steam that previous container for evaporation 11 produces, first container for evaporation 11 that the vapour outlet 6 of initial steam generation container connects is that the steam that produces in the initial steam generation container is carried out condensation), condensed water of condensation can directly be discharged, also can collect, be used for the equipment that other needs water; Its second effect then is when the steam that previous container for evaporation 11 is produced carries out condensation, also the heparin sodium waste liquid in self cavity volume heated concentratedly, produces steam then the heparin sodium waste liquids in the next container for evaporation 11 are heated.Each container for evaporation 11 is provided with the concentrated solution discharge outlet, after the heparin sodium waste liquid is concentrated to suitable concentration, discharges from the concentrated solution discharge outlet, handles through oven dry, can obtain protein fodder.
For under the situation of not setting up other heating unit, can make the heparin sodium waste liquid boiling in each container for evaporation 11, the inner chamber of described a plurality of container for evaporation 11 is negative pressure, and the internal pressure of first container for evaporation 11 that the vapour outlet 6 of initial steam generation container connects is less than the pressure of containing liquid exocoel 3 in the initial steam generation container; And on the flow direction of steam, the chamber pressure of container for evaporation 11 that is positioned at the place ahead is greater than the chamber pressure of the container for evaporation 11 that is positioned at the rear.Like this, just can guarantee that each container for evaporation 11 establishes under the situation of other heating unit in addition not needing, and make the heparin sodium waste liquid boiling in self inner volume, reduce the consumption of the energy.
Claims (7)
1. heparin sodium waste liquor treatment equipment, it is characterized in that: comprise the initial steam generation container that is used for evaporation concentration heparin sodium waste liquid, described initial steam generation container has seal isolation inner casing (4) and outer cavity shell (5), seal isolation inner casing (4) is fixedly installed in the outer cavity shell (5), in the seal isolation inner casing (4) is heating bore (2), be Sheng liquid exocoel (3) between seal isolation inner casing (4) and the outer cavity shell (5), in heating bore (2), be provided with heating unit (1), the heparin sodium waste liquid is contained in the liquid exocoel (3), outer cavity shell (5) is provided with vapour outlet (6) and liquid-inlet (7), and outer cavity shell (5) bottom is provided with concentrated solution discharge outlet (8).
2. heparin sodium waste liquor treatment equipment as claimed in claim 1 is characterized in that: be negative pressure in the described Sheng liquid exocoel (3).
3. heparin sodium waste liquor treatment equipment as claimed in claim 2 is characterized in that: in heating bore (2), be provided with two ends and be fixedly connected on heat transfer tube (9) on the seal isolation inner casing (4), and the two ends of heat transfer tube (9) all with contain liquid exocoel (3) and communicate.
4. heparin sodium waste liquor treatment equipment as claimed in claim 3, it is characterized in that: cavity shell (5) is provided with fume emission mouth (12) outside, seal isolation inner casing (4) is provided with the smoke exhaust pipe (10) that is communicated with fume emission mouth (12) and heating bore (2), the one end sealing of described smoke exhaust pipe (10) is arranged on fume emission mouth (12) and locates, and the other end sealing is arranged on the seal isolation inner casing (4).
5. heparin sodium waste liquor treatment equipment as claimed in claim 4 is characterized in that: described smoke exhaust pipe (10) is the coiling shape.
6. according to the described heparin sodium waste liquor treatment equipment of any claim in the claim 1 to 5, it is characterized in that: the vapour outlet of described initial steam generation container (6) is connected in series with a plurality of container for evaporation (11) by pipeline.
7. heparin sodium waste liquor treatment equipment as claimed in claim 6, it is characterized in that: the inner chamber of described a plurality of container for evaporation (11) is negative pressure, and the internal pressure of first container for evaporation (11) that the vapour outlet (6) of initial steam generation container connects is less than the pressure of containing liquid exocoel (3) in the initial steam generation container; And on the flow direction of steam, the chamber pressure of container for evaporation (11) that is positioned at the place ahead is greater than the chamber pressure of the container for evaporation that is positioned at the rear (11).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201865462U CN202089859U (en) | 2011-06-03 | 2011-06-03 | Heparin sodium waste liquid treatment equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201865462U CN202089859U (en) | 2011-06-03 | 2011-06-03 | Heparin sodium waste liquid treatment equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202089859U true CN202089859U (en) | 2011-12-28 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011201865462U Expired - Fee Related CN202089859U (en) | 2011-06-03 | 2011-06-03 | Heparin sodium waste liquid treatment equipment |
Country Status (1)
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|---|---|
| CN (1) | CN202089859U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102285696A (en) * | 2011-06-03 | 2011-12-21 | 四川泓乾生物科技有限公司 | Treatment equipment and method of liquaemin waste liquid |
-
2011
- 2011-06-03 CN CN2011201865462U patent/CN202089859U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102285696A (en) * | 2011-06-03 | 2011-12-21 | 四川泓乾生物科技有限公司 | Treatment equipment and method of liquaemin waste liquid |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20111228 Termination date: 20140603 |