CN104324530A - Waste alcohol sediment separation device for sausage casing residues - Google Patents
Waste alcohol sediment separation device for sausage casing residues Download PDFInfo
- Publication number
- CN104324530A CN104324530A CN201410579876.6A CN201410579876A CN104324530A CN 104324530 A CN104324530 A CN 104324530A CN 201410579876 A CN201410579876 A CN 201410579876A CN 104324530 A CN104324530 A CN 104324530A
- Authority
- CN
- China
- Prior art keywords
- tank
- alcohol
- precipitation
- tank body
- waste
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 title claims abstract description 83
- 239000002699 waste material Substances 0.000 title claims abstract description 52
- 238000000926 separation method Methods 0.000 title claims abstract description 8
- 239000013049 sediment Substances 0.000 title abstract 9
- 235000013580 sausages Nutrition 0.000 title 1
- 238000003795 desorption Methods 0.000 claims abstract description 19
- HTTJABKRGRZYRN-UHFFFAOYSA-N Heparin Chemical compound OC1C(NC(=O)C)C(O)OC(COS(O)(=O)=O)C1OC1C(OS(O)(=O)=O)C(O)C(OC2C(C(OS(O)(=O)=O)C(OC3C(C(O)C(O)C(O3)C(O)=O)OS(O)(=O)=O)C(CO)O2)NS(O)(=O)=O)C(C(O)=O)O1 HTTJABKRGRZYRN-UHFFFAOYSA-N 0.000 claims abstract description 18
- 229960002897 heparin Drugs 0.000 claims abstract description 18
- 229920000669 heparin Polymers 0.000 claims abstract description 18
- 238000004064 recycling Methods 0.000 claims abstract description 11
- 238000007599 discharging Methods 0.000 claims abstract description 7
- 238000001556 precipitation Methods 0.000 claims description 59
- 238000011084 recovery Methods 0.000 claims description 20
- 238000005086 pumping Methods 0.000 claims description 19
- 239000002893 slag Substances 0.000 claims description 2
- 239000007788 liquid Substances 0.000 abstract description 8
- 238000004519 manufacturing process Methods 0.000 abstract description 8
- 239000000243 solution Substances 0.000 abstract description 6
- 239000011259 mixed solution Substances 0.000 abstract description 2
- 238000004062 sedimentation Methods 0.000 abstract 6
- 238000004134 energy conservation Methods 0.000 abstract 1
- 238000005119 centrifugation Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
Landscapes
- Degasification And Air Bubble Elimination (AREA)
Abstract
The invention relates to a heparin sediment and waste alcohol separation device. The heparin sediment and waste alcohol separation device comprises a desorption tank, an alcohol sedimentation tank, a waste alcohol storage tank, a gas storage tank and a vacuum pump, wherein the lower end of the desorption tank is connected with the upper end of the alcohol sedimentation tank by a pipeline; the upper end of the alcohol sedimentation tank is provided with a vacuumizing pipe and the other end of the vacuumizing pipe is connected with the upper end of the gas storage tank; the upper end of the gas storage tank is connected with the vacuum pump by a pipeline; a waste alcohol recycling pipe is arranged at the position, close to the lower end, of one side of the alcohol sedimentation tank; the waste alcohol recycling pipe is communicated to the upper end of the waste alcohol storage tank and is provided with a conveying pump; the lower end of the alcohol sedimentation tank is provided with a sediment discharging pipe; the sediment discharging pipe is provided with a discharging valve; and a sediment recycling bucket is arranged at the lower end of the sediment discharging pipe. The heparin sediment and waste alcohol separation device has the advantages that desorption liquid can be rapidly and sufficiently conveyed to the sedimentation tank and the production efficiency is improved; an alcohol and heparin sediment mixed solution can be effectively separated on the basis of omission of a power device, and an alcohol solution is recycled in time; and energy conservation and emission reduction can be realized, and the production cost can be effectively reduced.
Description
Technical field
The present invention relates to heparin precipitation and its waste alcohol separation field, be specifically related to a kind of heparin precipitation and its waste alcohol separator.
Background technology
In heparin production process, be adsorbed with the resin of heparin after desorption, during alcohol settling heparin, desorption liquid arrives settling tank needs to affect production efficiency for a long time and desorption liquid not easily enters settling tank being adsorbed in resin, affects output, repeats and just increase production cost; After alcohol settling terminates, general by centrifugal mode in the separation of produced that waste alcohol and heparin precipitate, but containing a large amount of salt in precipitated liquid, larger to centrifugation apparatus corrosivity, and centrifugal postheparin easily loses when reclaiming, the operation of dismounting centrifugation apparatus is also very loaded down with trivial details, and the power of centrifugation apparatus is comparatively large, increases production cost.
Summary of the invention
In order to solve the problem, the present invention proposes a kind of heparin precipitation and its waste alcohol separator, simplicity of design is ingenious, easy to use, desorption liquid can either be made to be transported to settling tank fast fully enhance productivity, can after precipitation terminates, waste alcohol be effectively made to be separated with heparin again, simple to operate, and can production cost be effectively reduced.
In order to reach foregoing invention object, the present invention proposes following technical scheme:
Heparin precipitation and its waste alcohol separator, it comprises desorption tank, alcohol precipitation tank, waste alcohol storage tank, air accumulator and vavuum pump, desorption tank lower end is connected to alcohol precipitation tank upper end by pipeline, vacuum-pumping tube is equipped with in alcohol precipitation tank upper end, the other end of vacuum-pumping tube connects air accumulator upper end, side, air accumulator upper end connects vavuum pump by pipeline, alcohol precipitation tank side is near lower end position waste alcohol recovery tube, waste alcohol recovery tube leads to waste alcohol storage tank upper end, and waste alcohol recovery tube is equipped with delivery pump, precipitation delivery pipe is equipped with in alcohol precipitation tank lower end, precipitation delivery pipe is equipped with drain valve, precipitation recycling bin is equipped with in precipitation delivery pipe lower end.
Described alcohol precipitation tank comprises drive motors, shaft, paddle, manhole, tank body, tank body upper end is cylindric tank body, lower end is cone-shaped tank body, cone-shaped tank body is connected to cylindric tank body lower end, drive motors is equipped with in cylindric tank body upper end, drive motors lower end connects shaft, shaft gos deep into tank interior through tank body upper end, the shaft of tank interior is equipped with paddle, waste alcohol recovery tube is equipped with in lower end, cylindric tank body side, waste alcohol recovery tube leads to waste alcohol storage tank upper end, and waste alcohol recovery tube is equipped with delivery pump, side, cylindric tank body upper end connects desorption tank by pipeline, cylindric tank body upper end opposite side connects air accumulator by vacuum-pumping tube, cylindric tank body upper end also has manhole, manhole is stamped manhole cover, precipitation delivery pipe is equipped with in cone-shaped tank body lower end, precipitation delivery pipe is equipped with drain valve, precipitation recycling bin is equipped with in precipitation delivery pipe lower end.
Described side, air accumulator upper end connects vacuum-pumping tube, and vacuum-pumping tube gos deep into tank body of air storage tank inner bottom part through air accumulator upper end, and side, air accumulator upper end is also connected with vavuum pump by pipeline, and residul discharging valve is equipped with in air accumulator lower end.Observation visor vacuum-pumping tube is equipped with.
Advantage of the present invention is that simplicity of design is ingenious, easy to use, desorption liquid can either be made to be transported to settling tank fast fully enhance productivity, on the basis of reducing power set, effectively alcohol and heparin can be precipitated mixed solution to be again separated, timely recovery waste alcohol solution, plays energy-saving and emission-reduction and effectively reduces production cost effect.
Accompanying drawing explanation
Fig. 1 is schematic diagram of the present invention.
Detailed description of the invention
In order to the present invention is further described, introduce below in conjunction with Figure of description:
With reference to accompanying drawing 1, heparin precipitation and its waste alcohol separator, it comprises desorption tank 1, alcohol precipitation tank 2, waste alcohol storage tank 3, air accumulator 4 and vavuum pump 5, desorption tank 1 lower end is connected to alcohol precipitation tank 2 upper end by pipeline, vacuum-pumping tube is equipped with in alcohol precipitation tank 2 upper end, the other end of vacuum-pumping tube connects air accumulator 4 upper end, side, air accumulator 4 upper end connects vavuum pump 5 by pipeline, alcohol precipitation tank 2 side is near lower end position waste alcohol recovery tube, waste alcohol recovery tube leads to waste alcohol storage tank 3 upper end, and waste alcohol recovery tube is equipped with delivery pump 6, precipitation delivery pipe is equipped with in alcohol precipitation tank 2 lower end, precipitation delivery pipe is equipped with drain valve 7, precipitation recycling bin 8 is equipped with in precipitation delivery pipe lower end.
Described alcohol precipitation tank 2 comprises drive motors 21, shaft 22, paddle 23, manhole 24, tank body, tank body upper end is cylindric tank body 25, lower end is cone-shaped tank body 26, cone-shaped tank body 26 is connected to cylindric tank body 25 lower end, drive motors 21 is equipped with in cylindric tank body 25 upper end, drive motors 21 lower end connects shaft 22, shaft 22 gos deep into tank interior through tank body upper end, the shaft 22 of tank interior is equipped with paddle 23, waste alcohol recovery tube is equipped with in lower end, cylindric tank body 25 side, waste alcohol recovery tube leads to waste alcohol storage tank 3 upper end, and waste alcohol recovery tube is equipped with delivery pump 6, side, cylindric tank body 25 upper end connects desorption tank 1 by pipeline, cylindric tank body 25 upper end opposite side connects air accumulator 4 by vacuum-pumping tube, cylindric tank body 25 upper end also has manhole 24, manhole is stamped manhole cover, precipitation delivery pipe is equipped with in cone-shaped tank body 26 lower end, precipitation delivery pipe is equipped with drain valve 7, precipitation recycling bin 8 is equipped with in precipitation delivery pipe lower end.
Described side, air accumulator 4 upper end connects vacuum-pumping tube, and vacuum-pumping tube gos deep into tank body of air storage tank inner bottom part through air accumulator 4 upper end, and side, air accumulator upper end is also connected with vavuum pump 5 by pipeline, and residul discharging valve 41 is equipped with in air accumulator 4 lower end.Vacuum-pumping tube is equipped with and observes visor 42.
When the present invention uses, vavuum pump startup vacuumizes air accumulator, indirectly also be pumped into negative pressure in alcohol precipitation tank like this, desorption liquid in such desorption tank is under negative-pressure sucking effect, in suction alcohol precipitation tank, observed until when not having liquid to pass through by the observation visor be arranged in vacuum-pumping pipeline, stop vavuum pump, to blind off a line valve, alcohol precipitation tank starts drive motors and starts to precipitate heparin, stir after 20 to 30 minutes, stop stirring, solution is made to start layering, be deposited to cone-shaped tank body, waste alcohol solution is on upper strata, open manhole like this, floating one deck impurity is above fished for away, start the delivery pump on waste alcohol recovery tube, waste alcohol solution is transported in waste alcohol storage tank, etc. pending recycling, finally the drain valve on precipitation delivery pipe is opened, precipitation solution containing a small amount of waste alcohol is put into precipitation recycling bin, precipitation reclaim etc. pending, process end, manhole cover is closed, drain valve cuts out, delivery pump also ensures to stop, whole device can carry out next round repeated work.
Claims (3)
1. heparin precipitation and its waste alcohol separator, it comprises desorption tank, alcohol precipitation tank, waste alcohol storage tank, air accumulator and vavuum pump, it is characterized in that desorption tank lower end is connected to alcohol precipitation tank upper end by pipeline, vacuum-pumping tube is equipped with in alcohol precipitation tank upper end, the other end of vacuum-pumping tube connects air accumulator upper end, side, air accumulator upper end connects vavuum pump by pipeline, alcohol precipitation tank side is near lower end position waste alcohol recovery tube, waste alcohol recovery tube leads to waste alcohol storage tank upper end, and waste alcohol recovery tube is equipped with delivery pump, precipitation delivery pipe is equipped with in alcohol precipitation tank lower end, precipitation delivery pipe is equipped with drain valve, precipitation recycling bin is equipped with in precipitation delivery pipe lower end.
2. heparin precipitation according to claim 1 and its waste alcohol separator, it is characterized in that described alcohol precipitation tank comprises drive motors, shaft, paddle, manhole, tank body, tank body upper end is cylindric tank body, lower end is cone-shaped tank body, cone-shaped tank body is connected to cylindric tank body lower end, drive motors is equipped with in cylindric tank body upper end, drive motors lower end connects shaft, shaft gos deep into tank interior through tank body upper end, the shaft of tank interior is equipped with paddle, waste alcohol recovery tube is equipped with in lower end, cylindric tank body side, waste alcohol recovery tube leads to waste alcohol storage tank upper end, and waste alcohol recovery tube is equipped with delivery pump, side, cylindric tank body upper end connects desorption tank by pipeline, cylindric tank body upper end opposite side connects air accumulator by vacuum-pumping tube, cylindric tank body upper end also has manhole, manhole is stamped manhole cover, precipitation delivery pipe is equipped with in cone-shaped tank body lower end, precipitation delivery pipe is equipped with drain valve, precipitation recycling bin is equipped with in precipitation delivery pipe lower end.
3. waste alcohol precipitation separation device in casing slag according to claim 1, it is characterized in that described side, air accumulator upper end connects vacuum-pumping tube, vacuum-pumping tube gos deep into tank body of air storage tank inner bottom part through air accumulator upper end, side, air accumulator upper end is also connected with vavuum pump by pipeline, residul discharging valve is equipped with in air accumulator lower end, vacuum-pumping tube is equipped with observation visor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410579876.6A CN104324530B (en) | 2014-10-27 | 2014-10-27 | Waste alcohol precipitation separation device in casing slag |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410579876.6A CN104324530B (en) | 2014-10-27 | 2014-10-27 | Waste alcohol precipitation separation device in casing slag |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104324530A true CN104324530A (en) | 2015-02-04 |
| CN104324530B CN104324530B (en) | 2016-08-03 |
Family
ID=52399409
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410579876.6A Active CN104324530B (en) | 2014-10-27 | 2014-10-27 | Waste alcohol precipitation separation device in casing slag |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104324530B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112517572A (en) * | 2020-11-24 | 2021-03-19 | 刘睿峥 | System and method for mixing, cleaning and deslagging medium in settling tank |
| CN116711790A (en) * | 2023-06-15 | 2023-09-08 | 厦门荷蓬生物科技有限公司 | Device and process for preparing tea source element particles |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000312805A (en) * | 1999-04-28 | 2000-11-14 | Houshou:Kk | Turbid water treatment device |
| CN102989203A (en) * | 2012-08-21 | 2013-03-27 | 泰州市蓝海环保科技有限公司 | Mud and water separating equipment |
| CN203244812U (en) * | 2013-03-20 | 2013-10-23 | 南通天龙畜产品有限公司 | Heparin sodium precipitation and separation device |
| CN203613131U (en) * | 2013-10-28 | 2014-05-28 | 如皋市坝新肠衣有限公司 | Heparin sodium production device |
| CN203710747U (en) * | 2014-01-22 | 2014-07-16 | 广元市申达实业有限公司 | Heparin sodium sediment separation tank |
-
2014
- 2014-10-27 CN CN201410579876.6A patent/CN104324530B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000312805A (en) * | 1999-04-28 | 2000-11-14 | Houshou:Kk | Turbid water treatment device |
| CN102989203A (en) * | 2012-08-21 | 2013-03-27 | 泰州市蓝海环保科技有限公司 | Mud and water separating equipment |
| CN203244812U (en) * | 2013-03-20 | 2013-10-23 | 南通天龙畜产品有限公司 | Heparin sodium precipitation and separation device |
| CN203613131U (en) * | 2013-10-28 | 2014-05-28 | 如皋市坝新肠衣有限公司 | Heparin sodium production device |
| CN203710747U (en) * | 2014-01-22 | 2014-07-16 | 广元市申达实业有限公司 | Heparin sodium sediment separation tank |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112517572A (en) * | 2020-11-24 | 2021-03-19 | 刘睿峥 | System and method for mixing, cleaning and deslagging medium in settling tank |
| CN116711790A (en) * | 2023-06-15 | 2023-09-08 | 厦门荷蓬生物科技有限公司 | Device and process for preparing tea source element particles |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104324530B (en) | 2016-08-03 |
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| PB01 | Publication | ||
| EXSB | Decision made by sipo to initiate substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |