CN205461060U - Forced circulation sprays evaporimeter - Google Patents
Forced circulation sprays evaporimeter Download PDFInfo
- Publication number
- CN205461060U CN205461060U CN201620227933.9U CN201620227933U CN205461060U CN 205461060 U CN205461060 U CN 205461060U CN 201620227933 U CN201620227933 U CN 201620227933U CN 205461060 U CN205461060 U CN 205461060U
- Authority
- CN
- China
- Prior art keywords
- heat exchanger
- separator
- forced circulation
- cooling water
- feed liquid
- 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.)
- Active
Links
Abstract
The utility model relates to a forced circulation sprays evaporimeter. The problem that the energy consumption is big, treatment cost is high when mainly having solved current evaporimeter to the high raw material handling of concentration. A forced circulation sprays evaporimeter, its raw materials goes out feed liquid heat exchanger, steam condensate water raw materials heat exchanger, heater, separator, condenser and condensate water storage tank and connects gradually, the raw materials goes out the feed liquid heat exchanger and still is connected with but water heat exchanger of ejection of compact liquid cooling, the separator is connected with separator forced circulation pipeline, forced circulation pump and separator play steam pipe way, separator forced circulation pipeline is located separator upper portion position and is provided with spray set, spray set is located separator inner chamber upper portion. This forced circulation sprays evaporimeter simple structure is reasonable, and is practical convenient, easily promotes.
Description
Technical field
This utility model relates to vaporizer technology field, is specifically related to a kind of forced circulation spraying evaporator.
Background technology
Evaporation is exactly the method with heating, the solution containing fixedness solute is heated to boiling situation, makes partial solvent vaporize and be removed, thus improves the unit operation of solute concentration in solvent.Commercial production is applied evaporation operation have following several occasion:
1. concentrating dilute solution is directly produced product or concentrated solution reprocessing (such as crystallisation by cooling) is produced solid product, the such as concentration of electrolytic caustic soda liquid, the concentration of sugar water solution and the concentration etc. of various fruit juice；
Concentrate solution the most simultaneously and recycling design, the such as concentration of organophosphorus pesticide benzole soln take off benzene, the evaporation etc. of ethanol leachate in Chinese medicine production；
3. in order to obtain pure solvent, such as desalinization etc..
In a word, in the industry such as chemical industry, food industry, pharmacy, evaporation operation is widely used.
The raw material (such as fruit jam, saccharide etc.) bigger for viscosity and the higher raw material of some de-water ratios are (such as Aqueous Solutions of Polyethylene Glycol, initial moisture content is 8%, after needing moisture removal, water content is less than 1%), when concentration is the highest, moisture evaporation separating difficulty is the biggest, when removing with traditional vaporizer, energy consumption is big, evaporation time is long, and operation is loaded down with trivial details, and processing cost is high.
Utility model content
In order to overcome the deficiency of background technology, this utility model provides a kind of forced circulation spraying evaporator, when mainly solving the existing vaporizer Feedstock treating high to concentration, energy consumption is big, the problem that processing cost is high, this forced circulation spraying evaporator is simple and reasonable, in separator, forced circulation outlet uses spray form design, the external surface area of evaporation is considerably increased by the way of spray, thus significantly more efficient remove moisture removal, also evaporation time is substantially reduced, thus greatly reduce processing cost, technique is more succinct, workable, decrease operator, thus decrease cost of investment and operating cost.
This utility model be the technical scheme is that a kind of forced circulation spraying evaporator, it includes that raw material out-feed liquid heat exchanger, steam condensate (SC) raw material heat exchanger, heater, separator, condenser, condensed water storage tank and out-feed liquid cooling water heat exchanger, described raw material out-feed liquid heat exchanger, steam condensate (SC) raw material heat exchanger, heater, separator, condenser and condensed water storage tank are sequentially connected with；Described raw material out-feed liquid heat exchanger is also associated with out-feed liquid cooling water heat exchanger；Described raw material out-feed liquid heat exchanger connects feedstock pipeline, and described feedstock pipeline is provided with feed pump；Described separator connects separator forced circulation pipeline, forced circulation pump and separator steam outlet pipe road；Described separator forced circulation pipeline one end is connected to separator bottom, and the other end is connected to separator top；It is provided with forced circulation pump and heater on described separator forced circulation pipeline；Described separator forced circulation pipeline is positioned at separator upper position and is provided with spray equipment；Described spray equipment is positioned at interior separator cavity top；Described separator forced circulation pipeline is also associated with connecting raw material out-feed liquid heat exchanger；One end, described separator steam outlet pipe road is connected to separator top, and the other end connects upper end of condenser；Described heater connects steam steam inlet pipe road；It is provided with steam control valve and Pressure gauge on described steam steam inlet pipe road；Described raw material out-feed liquid heat exchanger, steam condensate (SC) raw material heat exchanger and out-feed liquid cooling water heat exchanger are plate type heat exchanger；Described heater is baffle heater；Described condenser is plate-type condenser；Described separator is provided with piezometer, thermometer and magnetic flap level gauge；Described condenser connects condenser cooling water inlet channel, condenser cooling water outlet conduit and condenser condensing water conduit；Described condenser cooling water inlet channel is connected to condenser lower end；Described condenser cooling water outlet conduit is connected to upper end of condenser；Described condenser condensing water conduit one end is connected to condenser lower end, and the other end is connected to condensed water storage tank upper end；The steam condensate (SC) that described heater produces imports condensed water storage tank after steam condensate (SC) raw material heat exchanger heat exchange；Described condensed water storage tank connects condensed water storage tank outlet conduit, vacuum system；Described condensed water storage tank outlet conduit is connected to condensed water tank bottom, and described condensed water storage tank outlet conduit has condensate pump；Described vacuum system is connected to condensed water tank top；Described condensed water storage tank is provided with liquidometer；Described out-feed liquid cooling water heat exchanger connects out-feed liquid cooling water heat exchanger cooling water inlet pipe road, out-feed liquid cooling water heat exchanger cooling water outlet pipe road and material outlet pipeline；Described out-feed liquid cooling water heat exchanger cooling water inlet pipe road is connected to out-feed liquid cooling water heat exchanger lower end；Described out-feed liquid cooling water heat exchanger cooling water outlet pipe road is connected to out-feed liquid cooling water heat exchanger upper end, and described material outlet pipeline is provided with thermometer.
The beneficial effects of the utility model are: owing to taking technique scheme, this forced circulation spraying evaporator is simple and reasonable, in separator, forced circulation outlet uses spray form design, considerably increases the external surface area of evaporation by the way of spray, thus significantly more efficient removes moisture removal, also evaporation time is substantially reduced, thus greatly reducing processing cost, technique is more succinct, workable, decrease operator, thus decrease cost of investment and operating cost.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In figure 100, raw material out-feed liquid heat exchanger；110, feedstock pipeline；120, feed pump；200, steam condensate (SC) raw material heat exchanger；300, heater；310, steam steam inlet pipe road；400, separator；410, separator forced circulation pipeline；411, spray equipment；420, forced circulation pump；430, separator steam outlet pipe road；500, condenser；510, condenser cooling water inlet channel；520, condenser cooling water outlet conduit；600, condensed water storage tank；610, condensed water storage tank outlet conduit；620, vacuum system；700, out-feed liquid cooling water heat exchanger；710, out-feed liquid cooling water heat exchanger cooling water inlet pipe road；720, out-feed liquid cooling water heat exchanger cooling water outlet pipe road；730, material outlet pipeline.
Detailed description of the invention
Below in conjunction with the accompanying drawings this utility model embodiment is described further:
As it is shown in figure 1, a kind of forced circulation spraying evaporator, it includes raw material out-feed liquid heat exchanger 100, steam condensate (SC) raw material heat exchanger 200, heater 300, separator 400, condenser 500, condensed water storage tank 600 and out-feed liquid cooling water heat exchanger 700.
Described raw material out-feed liquid heat exchanger 100, steam condensate (SC) raw material heat exchanger 200, heater 300, separator 400, condenser 500 and condensed water storage tank 600 are sequentially connected with；Described raw material out-feed liquid heat exchanger 100 is also associated with out-feed liquid cooling water heat exchanger 700；Described raw material out-feed liquid heat exchanger 100, steam condensate (SC) raw material heat exchanger 200 and out-feed liquid cooling water heat exchanger 700 are plate type heat exchanger；Described heater 300 is baffle heater；Described condenser 500 is plate-type condenser；Described raw material out-feed liquid heat exchanger 100 connects feedstock pipeline 110, and described feedstock pipeline 110 is provided with feed pump 120.
Described heater 300 connects steam steam inlet pipe road 310；It is provided with steam control valve and Pressure gauge on described steam steam inlet pipe road 310.
Described separator 400 connects separator forced circulation pipeline 410, forced circulation pump 420 and separator steam outlet pipe road 430；Described separator forced circulation pipeline 410 one end is connected to bottom separator 400, and the other end is connected to separator 400 top；It is provided with forced circulation pump 420 and heater 300 on described separator forced circulation pipeline 410；Described separator forced circulation pipeline 410 is positioned at separator 400 upper position and is provided with spray equipment 411；Described spray equipment 411 is positioned at separator 400 inner chamber top；Described spray equipment 411 considerably increases the external surface area of evaporation by the way of spray, thus significantly more efficient removes moisture removal, also substantially reduces evaporation time, and described separator forced circulation pipeline 410 is also associated with connecting raw material out-feed liquid heat exchanger 100；One end, described separator steam outlet pipe road 430 is connected to separator 400 top, and the other end connects condenser 500 upper end；Described separator 400 is provided with piezometer, thermometer and magnetic flap level gauge.
Described condenser 500 connects condenser cooling water inlet channel 510, condenser cooling water outlet conduit 520 and condenser condensing water conduit；Described condenser cooling water inlet channel 510 is connected to condenser 500 lower end；Described condenser cooling water outlet conduit 520 is connected to condenser 500 upper end；Described condenser condensing water conduit one end is connected to condenser 500 lower end, and the other end is connected to condensed water storage tank 600 upper end；The steam condensate (SC) that described heater 300 produces imports condensed water storage tank 600 after steam condensate (SC) raw material heat exchanger 200 heat exchange.
Described condensed water storage tank 600 connects condensed water storage tank outlet conduit 610, vacuum system 620；Described condensed water storage tank outlet conduit 610 is connected to bottom condensed water storage tank 600, and described condensed water storage tank outlet conduit 610 has condensate pump；Described vacuum system 620 is connected to condensed water storage tank 600 top；Described condensed water storage tank 600 is provided with liquidometer.
Described out-feed liquid cooling water heat exchanger 700 connects out-feed liquid cooling water heat exchanger cooling water inlet pipe road 710, out-feed liquid cooling water heat exchanger cooling water outlet pipe road 720 and material outlet pipeline 730；Described out-feed liquid cooling water heat exchanger cooling water inlet pipe road 710 is connected to out-feed liquid cooling water heat exchanger 700 lower end；Described out-feed liquid cooling water heat exchanger cooling water outlet pipe road 720 is connected to out-feed liquid cooling water heat exchanger 700 upper end, and described material outlet pipeline 730 is provided with thermometer.
Every technical staff's notice: although this utility model describes according to above-mentioned detailed description of the invention; but invention thought of the present utility model is not limited to that utility model; the repacking of any utilization inventive concept, all will include in this patent scope of patent protection.
Claims (7)
1. a forced circulation spraying evaporator, including raw material out-feed liquid heat exchanger, steam condensate (SC) raw material heat exchanger, heater, separator, condenser, condensed water storage tank and out-feed liquid cooling water heat exchanger, it is characterised in that: described raw material out-feed liquid heat exchanger, steam condensate (SC) raw material heat exchanger, heater, separator, condenser and condensed water storage tank are sequentially connected with；Described raw material out-feed liquid heat exchanger is also associated with out-feed liquid cooling water heat exchanger；Described raw material out-feed liquid heat exchanger connects feedstock pipeline, and described feedstock pipeline is provided with feed pump；Described separator connects separator forced circulation pipeline, forced circulation pump and separator steam outlet pipe road；Described separator forced circulation pipeline one end is connected to separator bottom, and the other end is connected to separator top；It is provided with forced circulation pump and heater on described separator forced circulation pipeline；Described separator forced circulation pipeline is positioned at separator upper position and is provided with spray equipment；Described spray equipment is positioned at interior separator cavity top；Described separator forced circulation pipeline is also associated with connecting raw material out-feed liquid heat exchanger；One end, described separator steam outlet pipe road is connected to separator top, and the other end connects upper end of condenser.
A kind of forced circulation spraying evaporator the most according to claim 1, it is characterised in that: described heater connects steam steam inlet pipe road；It is provided with steam control valve and Pressure gauge on described steam steam inlet pipe road.
A kind of forced circulation spraying evaporator the most according to claim 1, it is characterised in that: described raw material out-feed liquid heat exchanger, steam condensate (SC) raw material heat exchanger and out-feed liquid cooling water heat exchanger are plate type heat exchanger；Described heater is baffle heater；Described condenser is plate-type condenser.
A kind of forced circulation spraying evaporator the most according to claim 1, it is characterised in that: described separator is provided with piezometer, thermometer and magnetic flap level gauge.
A kind of forced circulation spraying evaporator the most according to claim 1, it is characterised in that: described condenser connects condenser cooling water inlet channel, condenser cooling water outlet conduit and condenser condensing water conduit；Described condenser cooling water inlet channel is connected to condenser lower end；Described condenser cooling water outlet conduit is connected to upper end of condenser；Described condenser condensing water conduit one end is connected to condenser lower end, and the other end is connected to condensed water storage tank upper end；The steam condensate (SC) that described heater produces imports condensed water storage tank after steam condensate (SC) raw material heat exchanger heat exchange.
A kind of forced circulation spraying evaporator the most according to claim 1, it is characterised in that: described condensed water storage tank connects condensed water storage tank outlet conduit, vacuum system；Described condensed water storage tank outlet conduit is connected to condensed water tank bottom, and described condensed water storage tank outlet conduit has condensate pump；Described vacuum system is connected to condensed water tank top；Described condensed water storage tank is provided with liquidometer.
A kind of forced circulation spraying evaporator the most according to claim 1, it is characterised in that: described out-feed liquid cooling water heat exchanger connects out-feed liquid cooling water heat exchanger cooling water inlet pipe road, out-feed liquid cooling water heat exchanger cooling water outlet pipe road and material outlet pipeline；Described out-feed liquid cooling water heat exchanger cooling water inlet pipe road is connected to out-feed liquid cooling water heat exchanger lower end；Described out-feed liquid cooling water heat exchanger cooling water outlet pipe road is connected to out-feed liquid cooling water heat exchanger upper end, and described material outlet pipeline is provided with thermometer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620227933.9U CN205461060U (en) | 2016-03-23 | 2016-03-23 | Forced circulation sprays evaporimeter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620227933.9U CN205461060U (en) | 2016-03-23 | 2016-03-23 | Forced circulation sprays evaporimeter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205461060U true CN205461060U (en) | 2016-08-17 |
Family
ID=56652221
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620227933.9U Active CN205461060U (en) | 2016-03-23 | 2016-03-23 | Forced circulation sprays evaporimeter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205461060U (en) |
-
2016
- 2016-03-23 CN CN201620227933.9U patent/CN205461060U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105861256B (en) | White wine removal of impurities purification system and method | |
| CN105251233A (en) | Falling film and MVR forced circulating evaporative crystallization system | |
| CN102952629B (en) | Technological method for extracting natural cinnamon oil | |
| CN101757802B (en) | Energy-saving device for extracting and concentrating traditional Chinese medicine under low-temperature by reduced-pressure method | |
| CN107008026A (en) | Nickel sulfate evaporative crystallization technique | |
| CN100342840C (en) | Chinese medicine liquid vacuum concentrating process and apparatus thereof | |
| CN105327518A (en) | Pentanediamine concentration system and method thereof | |
| CN104436724A (en) | Traditional Chinese medicine leaching liquid MVR concentration process | |
| CN105017054B (en) | Solvent recovering system for DMF (Dimethyl Formamide) saliferous wastewater | |
| CN205216256U (en) | Falling liquid film and MVR forced circulation evaporation crystal system | |
| CN105251226A (en) | Anti-scaling concentration treatment process of traditional Chinese medicine water extraction solution | |
| CN102249203A (en) | Phosphoric acid evaporation process and device thereof | |
| CN103253819A (en) | Device and production technology for treating ternary-monomer wastewater and extracting sodium sulfate | |
| CN201454122U (en) | Extraction solution concentration device | |
| CN202951265U (en) | Efficient evaporating crystallizer | |
| CN105218316A (en) | A kind of hollow fiber pervaporation membrane prepares the device and method of dehydrated alcohol | |
| CN204275519U (en) | A kind of Chinese medicine leaching liquid MVR enrichment facility | |
| CN204174031U (en) | The treatment unit of refuse leachate reverse osmosis dope | |
| CN203196359U (en) | Outer circulating evaporator used to extract Chinese herbal medicines | |
| CN205461060U (en) | Forced circulation sprays evaporimeter | |
| CN103908799A (en) | Extracting and concentrating all-in-one machine | |
| CN102512833A (en) | Horizontal-pipe falling-film evaporation method coupling distillation and device thereof | |
| CN206566525U (en) | Suitable for the efficient atmospheric low-temperature concentration systems of Chinese medicine liquid | |
| CN202315342U (en) | Horizontal pipe falling film evaporation tower | |
| CN205461078U (en) | Boil evaporimeter of organic gas condensing reflux device of height |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 325000 Zhenglou Industrial Zone, Wanquan Town, Pingyang County, Wenzhou City, Zhejiang Province Patentee after: Zhejiang central Connaught environmental Polytron Technologies Inc Address before: 325000 Zhenglou Industrial Zone, Wanquan Town, Pingyang County, Wenzhou City, Zhejiang Province Patentee before: WENZHOU HUANNUO EVAPORATOR CO., LTD. |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Forced circulation sprays evaporimeter Effective date of registration: 20200630 Granted publication date: 20160817 Pledgee: China Minsheng Banking Corp Wenzhou branch Pledgor: ZHEJIANG VNOR ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. Registration number: Y2020330000416 |