CN202876406U - Ethanol recycling thickener - Google Patents
Ethanol recycling thickener Download PDFInfo
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- CN202876406U CN202876406U CN 201220575687 CN201220575687U CN202876406U CN 202876406 U CN202876406 U CN 202876406U CN 201220575687 CN201220575687 CN 201220575687 CN 201220575687 U CN201220575687 U CN 201220575687U CN 202876406 U CN202876406 U CN 202876406U
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Abstract
The utility model discloses an ethanol recycling thickener which comprises a stock solution tank, a concentration tank, a distillation tower, a compressor, a heater and an infusion pump. The stock solution tank is connected with a nozzle in the concentration tank through the infusion pump and the heater, the top opening of the concentration tank is connected with the distillation tower, and the distillation tower is connected with a heating pipeline of the heater through the compressor; an outlet of the concentration tank is connected with a finished product pipeline, a pipeline at the outlet is simultaneously connected with the nozzle in the concentration tank through the heater, and a connecting pipeline between the stock solution tank and the heater is provided with a pre-heater; and an outlet of the heating pipeline of the heater is connected with an inlet of the heating pipeline of the pre-heater, the outlet of the heating pipeline of the heater is connected with an inlet of the heating pipeline of the heater, the outlet of the heating pipeline of the heater is connected with a liquid storage tank through a concentrating and cooling device and a pipeline in the liquid storage tank is connected with a vacuum device. Novel recycling and concentrating device capable of realizing the integration of recycling and concentrating is high in ethanol recovery efficiency, controllable in recycling concentration, simple in structure and reliable in operation.
Description
Technical field:
The utility model relates to a kind of Recycled ethanol and concentrated equipment, is applicable to chemical industry, food and pharmaceuticals industry.
Background technology:
Energy-saving and cost-reducing be enterprise existence this.Energy-conservation is strengthen with can management, the measure of taking technical feasible, reasonable in economy and environment and society to bear, loss and waste reducing as far as possible from production of energy to the consumption links utilize the energy more effectively and reasonably; Consumption reduction is to reduce to drop into, reduce the consumption in producing.Ethanol is as one of solvent the most frequently used in the pharmaceuticals industry, and its fancy price and huge use amount are disagreed with energy-saving and cost-reducing Business survival rule significantly, and therefore, under the prerequisite that does not affect production, the consumption that how to reduce ethanol seems particularly important.
Reducing the most direct way of ethanol consumption recycles it exactly.Have inefficiency and produce at present the upper ethanol reclaimer that uses, it is uncontrollable to reclaim concentration, and Recycled ethanol and concentrated medicament can not integrated defectives.
The utility model content
The utility model is intended to overcome above-mentioned deficiency, provides a kind of simple in structure, reliable, and the ethanol organic efficiency is high, and it is controlled to reclaim concentration, and can realize reclaiming, concentration integrated novel ethanol reclaims concentrator.
A kind of ethanol reclaims thickener, comprise original fluid container, concentration tank, destilling tower, compressor reducer, heater, infusion pump, original fluid container is through infusion pump, heater links to each other with shower nozzle in the concentration tank, the concentration tank upper shed is connected with destilling tower, the compressed device of destilling tower links to each other with the heating pipe line of heater, the concentration tank outlet links to each other with the finished product pipeline, outlet has the pipeline heater via to link to each other with shower nozzle in the concentration tank simultaneously, on the connecting line of original fluid container and heater preheater is arranged, the heating pipe line outlet of heater links to each other with the import of preheater heating pipe line, the outlet of preheater heating pipe line links to each other with fluid reservoir through the condensing cooling device, and fluid reservoir has pipeline to link to each other with vacuum plant.
Further, described destilling tower lower end is evaporator section, and the upper end is the temperature control section.
Further, described concentration tank gas outlet links to each other with compressor reducer through cyclone separator, and cyclone separator lower end liquid outlet links to each other with concentration tank.
Further, described original fluid container has heater.
Further, described vacuum plant is the water circulation vavuum pump.
The beneficial effects of the utility model have:
(1) the ethanol organic efficiency is high, and the recovery degree is controlled, reclaims concentration integrated.The alcohol that contains that equipment can be controlled in the steam by temperature, the vacuum of control destilling tower temperature control section is as required measured, and improves thickening efficiency; After the ethanol recovery is finished, also can contain the concentrated of water liquid.
(2) equipment has been realized the reasonable utilization of the energy, has reduced energy consumption.Equipment heats up to recovered steam by compressor reducer, and heats with it, has rationally utilized the energy, has reduced energy consumption, has shortened the equipment turnaround time, has improved production efficiency, has saved production cost.
(3) simple in structure, be easy to disassembly, cleaning, maintenance, non-environmental-pollution is applicable to the advantages such as suitability for industrialized production.
Description of drawings
Fig. 1 is the utility model structural representation.
Among the figure: 1-concentration tank, 2-liquid outlet, 3-shower nozzle, the 4-infusion pump, 5-finished product pipeline, 6-heater, the 7-compressor reducer, 8-cyclone separator, 9-destilling tower, the 10-evaporator section, 11-temperature control section, 12-thermometer, the 13-preheater, 14-original fluid container, 15-fluid reservoir, the 16-vacuum plant, 17-condensing cooling device, 18-gas outlet.
The specific embodiment
As shown in Figure 1, the utility model ethanol reclaims thickener, comprise original fluid container 14, concentration tank 1, destilling tower 9, compressor reducer 7, heater 6, infusion pump 4, original fluid container 14 is through infusion pump 4, shower nozzle 3 in heater 6 and the concentration tank 1 links to each other, concentration tank 1 upper shed is connected with destilling tower 9, destilling tower 9 compressed devices 7 link to each other with the heating pipe line of heater 6, concentration tank 1 outlet 2 links to each other with finished product pipeline 5, outlet 2 has pipeline heater via 6 to link to each other with shower nozzle 3 in the concentration tank simultaneously, on the connecting line of original fluid container 14 and heater 6 preheater 13 is arranged, the heating pipe line outlet of heater 6 links to each other with the import of preheater 13 heating pipe lines, the outlet of preheater 13 heating pipe lines links to each other with fluid reservoir 15 through condensing cooling device 17, and fluid reservoir 15 has pipeline to link to each other with vacuum plant 16.
Further, destilling tower 9 lower ends are evaporator section 10, and the upper end is temperature control section 11, and thermometer 12 is installed on the destilling tower 9.
Further, concentration tank 1 gas outlet 18 links to each other with compressor reducer 7 through cyclone separator 8, and cyclone separator 8 lower end liquid outlets link to each other with concentration tank 1.
Further, original fluid container 14 has heater, can heat pot liquid.
Further, vacuum plant 16 is the water circulation vavuum pump.
During use, the liquid in the original fluid container 14, enters in the concentration tank 1 through preheater 13, heater 6, shower nozzle 3 sprayings under infusion pump 4 effects a little after the heat successively through heater.During Recycled ethanol, gas enters compressor reducer 7 and heats up after destilling tower 9 evaporator sections 10 on top, temperature control section 11; Gas after the intensification is for heater 6 heating, after residual air is utilized for preheater 13, be cooled to liquid ethanol through condensing cooling device 17 and be stored in the fluid reservoir 15, unnecessary gas also can enter into the water circulation vavuum pump that links to each other with fluid reservoir 15 and use as recirculated water.After ethanol reclaims and finishes, contain the concentrated of water liquid, steam enters compressor reducer 7 behind cyclone separator 8 from gas outlet 18, heater via 6, preheater 13, condensing cooling device 17 are to fluid reservoir 15 again, recovered steam, simultaneously, concentrate is got back to the concentration tank 1 after infusion pump 4, heater 6, shower nozzle 3 sprayings from the liquid outlet 2 of concentration tank 1.Whole process loops, until after being concentrated into required degree, through 5 outputs of finished product pipeline.
Certainly; the utility model also can have other various embodiments; in the situation that does not deviate from the utility model spirit and essence thereof; those of ordinary skill in the art can make various corresponding changes and distortion according to the utility model, but these corresponding changes and distortion all should belong to the protection domain of the appended claim of the utility model.
Claims (5)
1. an ethanol reclaims thickener, it is characterized in that: comprise original fluid container (14), concentration tank (1), destilling tower (9), compressor reducer (7), heater (6), infusion pump (4), original fluid container (14) is through infusion pump (4), shower nozzle (3) in heater (6) and the concentration tank (1) links to each other, concentration tank (1) upper shed is connected with destilling tower (9), the compressed device of destilling tower (9) (7) links to each other with the heating pipe line of heater, concentration tank (1) outlet (2) links to each other with finished product pipeline (5), outlet (2) has pipeline heater via (6) to link to each other with the interior shower nozzle of concentration tank (1) (3) simultaneously, on the connecting line of original fluid container (14) and heater (6) preheater (13) is arranged, the heating pipe line outlet of heater (6) links to each other with the import of preheater (13) heating pipe line, the outlet of preheater (13) heating pipe line links to each other with fluid reservoir (15) through condensing cooling device (17), and fluid reservoir (15) has pipeline to link to each other with vacuum plant (16).
2. ethanol according to claim 1 reclaims thickener, and it is characterized in that: described destilling tower (9) lower end is evaporator section (10), and the upper end is temperature control section (11).
3. ethanol according to claim 1 reclaims thickener, and it is characterized in that: described concentration tank (1) gas outlet (18) links to each other with compressor reducer (7) through cyclone separator (8), and cyclone separator (8) lower end liquid outlet links to each other with concentration tank (1).
4. ethanol according to claim 1 reclaims thickener, and it is characterized in that: described original fluid container (14) has heater.
5. ethanol according to claim 1 reclaims thickener, and it is characterized in that: described vacuum plant is the water circulation vavuum pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220575687 CN202876406U (en) | 2012-11-02 | 2012-11-02 | Ethanol recycling thickener |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220575687 CN202876406U (en) | 2012-11-02 | 2012-11-02 | Ethanol recycling thickener |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202876406U true CN202876406U (en) | 2013-04-17 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220575687 Expired - Lifetime CN202876406U (en) | 2012-11-02 | 2012-11-02 | Ethanol recycling thickener |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202876406U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103920298A (en) * | 2014-04-30 | 2014-07-16 | 江西中医药大学 | Spray concentrator |
| CN104524789A (en) * | 2014-11-28 | 2015-04-22 | 悦康药业集团安徽天然制药有限公司 | Single-effect concentrated alcohol recovering apparatus |
-
2012
- 2012-11-02 CN CN 201220575687 patent/CN202876406U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103920298A (en) * | 2014-04-30 | 2014-07-16 | 江西中医药大学 | Spray concentrator |
| CN104524789A (en) * | 2014-11-28 | 2015-04-22 | 悦康药业集团安徽天然制药有限公司 | Single-effect concentrated alcohol recovering apparatus |
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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: 20170608 Address after: 330000 Nanchang high tech Industrial Development Zone, Nanchang, AI Bei Sihu Road, No. 688, building No. 8 Patentee after: JIANGXI HBKHPHARM PHARMACEUTICAL EQUIPMENT CO.,LTD. Address before: 610041 No. 29 Tian Xiao street, Chengdu, Sichuan, Wuhou District Co-patentee before: Ding Chenhui Patentee before: CHENGDU KEER PHARMACEUTICAL Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| CX01 | Expiry of patent term |
Granted publication date: 20130417 |
|
| CX01 | Expiry of patent term |