CN201777904U - High temperature crystallizer - Google Patents

High temperature crystallizer Download PDF

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Publication number
CN201777904U
CN201777904U CN2010202208266U CN201020220826U CN201777904U CN 201777904 U CN201777904 U CN 201777904U CN 2010202208266 U CN2010202208266 U CN 2010202208266U CN 201020220826 U CN201020220826 U CN 201020220826U CN 201777904 U CN201777904 U CN 201777904U
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CN
China
Prior art keywords
heat conducting
high temperature
heat
conductive rod
conducting plate
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.)
Expired - Lifetime
Application number
CN2010202208266U
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Chinese (zh)
Inventor
陈兆勇
温致平
王石
彭云龙
曾贤桂
何晋勇
李鸿江
谢璀
孙宁
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SHENZHEN BIBAO ENVIRONMENTAL PROTECTION SCIENCE AND TECHNOLOGY Co Ltd
SHENZHEN ENVIRONMENT ENGINEERING SCIENCE TECH CENTER
Original Assignee
SHENZHEN BIBAO ENVIRONMENTAL PROTECTION SCIENCE AND TECHNOLOGY Co Ltd
SHENZHEN ENVIRONMENT ENGINEERING SCIENCE TECH CENTER
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Application filed by SHENZHEN BIBAO ENVIRONMENTAL PROTECTION SCIENCE AND TECHNOLOGY Co Ltd, SHENZHEN ENVIRONMENT ENGINEERING SCIENCE TECH CENTER filed Critical SHENZHEN BIBAO ENVIRONMENTAL PROTECTION SCIENCE AND TECHNOLOGY Co Ltd
Priority to CN2010202208266U priority Critical patent/CN201777904U/en
Application granted granted Critical
Publication of CN201777904U publication Critical patent/CN201777904U/en
Anticipated expiration legal-status Critical
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/30Wastewater or sewage treatment systems using renewable energies
    • Y02W10/37Wastewater or sewage treatment systems using renewable energies using solar energy

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  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

A high temperature crystallizer for high-temperature blasting and evaporative crystallization of waste water or sea water in the form of liquid membranes comprises a body, wherein, a plurality of air guide holes serving as vapor channels are parallelly arranged in the body, a plurality of rows of heat conducting rods made of high-temperature resistant heat conducting material are arranged in the vertical direction of the air guide holes, the heat conducting rods are connected with a heating element through a heat conducting plate, the heat conducting plate is fixedly arranged on one side surface of the body, one end of each heat conducting rod is arranged on the heat conducting plate, the other end extends inside the body, and a plurality of heating pipes connected with the heat conducting rods are vertically arranged above or/and below the heat conducting rods. The utility model is simple and compact in structure, and effective in evaporation, and can ensure fast temperature rise.

Description

A kind of high temperature crystallization device
Technical field
The utility model relates to water treatment field, especially relate to a kind ofly evaporate after waste water or seawater are formed liquid film with the pressure reduction form, the high temperature crystallization device of crystallization treatment.
Background technology
Along with socioeconomic high development, the industrialization and the urbanization of human society increasingly sharpen, and water pollutes serious day by day.The sewage of a lot of unprocessed mistakes directly is discharged into rivers and lakes, make rivers and lakes slowly lose self-purification capacity, the first-generation water that formation is representative with black smelly anoxic pollutes, or form with heavy metal, the s-generation water that noxious chemical pollutes for representative pollutes, or formation is the third generation water pollution of representative with the pollution of nutritive element excess, more very be that the three generations pollutes simultaneously and occurs in a lot of rivers and lakes, make the rivers and lakes water of China pollute serious day by day, though various wastewater treatment equipments is arranged at present, but it is big more or less to exist floor space, investment and working cost height, low to organic pollutant removal efficient, take effect and wait problem slowly.
Sea water desaltination is the technology and the process of separating salt and water in the seawater.Sea water desaltination at present mainly comprise Re Fa and embrane method.Hot method sea water desaltination mainly contains multistage flash evaporation and two kinds of methods of low temperature multiple-effect distillation.The multistage flash evaporation complex treatment process, the cost height; And low temperature multiple-effect distillation is limited by the restriction of device volume, especially evaporation structure is huge, its internal sea water capacity is big, thereby heat up slowly, cause evaporation of seawater to be short of power, fail the latent heat of condensation of recovered steam in the whole in addition still-process, water vapour is not fully utilized, so the efficient of General System is not high, about below 35%.
The utility model content
The purpose of this utility model is to overcome the prior art defective, provides a kind of compact construction, evaporation soon, and is effective, is used for the high temperature evaporation crystallizer of waste water or brine disposal process.
The utility model is to realize like this, a kind of high temperature crystallization device, waste water or the seawater that is used for forming liquid film carries out the high temperature explosion, evaporative crystallization is handled, it comprises a body, parallel rows is shown a plurality of gas ports as vapour passage in the described body, in the vertical direction of described gas port, be arranged with the heat conductive rod of many rows, the making of a plurality of thermostable heat-conductive material composition; Described heat conductive rod is connected with heater by a heat-conducting plate.
Further, described heat-conducting plate is fixedly set in described body one side, and each heat conductive rod one end is loaded on the described heat-conducting plate, and the other end extends in the described body.
Or/and the below, also vertical row is shown a plurality of heating tubes that are connected with heat conductive rod to the utility model in described heat conductive rod top.
Further, be provided with nichrome wire in the described heating tube pipe.
Perhaps, described heating tube is a metal tube, is provided with nichrome wire in it.
The utility model structure design is simple, compactness, and heating is fast, and evaporation effect is good.
Description of drawings
Fig. 1 is the utility model example structure synoptic diagram;
Fig. 2 uses synoptic diagram for the utility model embodiment.
Embodiment
In order to make the purpose of this utility model, technical scheme and advantage clearer,, the utility model is further elaborated below in conjunction with drawings and Examples.Should be appreciated that specific embodiment described herein only in order to explanation the utility model, and be not used in qualification the utility model.
Referring to Fig. 1, the high temperature crystallization device 1 that the utility model provides is mainly used in the desalination of waste water or seawater and handles, its liquid film that is arranged at vaporizer 3 forms in the chamber 33, preliminary filtering waste water or seawater are injected in the liquid film producer 31 by the mechanical force high pressure of high-pressure pump, described liquid film producer 31 is provided with an annular spray frame, the support body upper end evenly is provided with the some high pressure spray nozzles that are interconnected, pumping into liquid film by high-pressure pump forms chamber 33 interior waste water or seawater and can be injected into vaporific by high pressure spray nozzle, it is the liquid film drop of 15-20 micron that the step-down outburst forms particle diameter, and the liquid film that falls within on the high temperature crystallization device 1 carries out the high temperature explosion by high temperature crystallization device 1 again, finish the evaporative crystallization treating processes.
Referring to Fig. 1, Fig. 2, the high temperature crystallization device 1 that the utility model provides comprises that one is made into circular or square body 11 by silicon nitride thermostable heat-conductive material, being covered with diameter on it is the straight-through aperture of 2-20 millimeter, be cellular, should straight-through aperture be gas port 12, passage as steam, spacing is the 5-10 millimeter between each gas port 2, with the vertical direction of gas port 12, transverse row is shown many rows, a plurality of long 1-2 rice, diameter 30-50 millimeter, by the solid heat conductive rod 13 that the thermostable heat-conductive material composition is made, described heat conductive rod 13 is connected with heating system 2 by a heat-conducting plate 14.Described heater 2 can be the sun power heat build-up system that is constituted by sun tracker and at least one condensor, the sunlight heat that is absorbed, compiled by condensor passes on each heat conductive rod 12 by heat-conducting plate 14, also can be other heat generating systems and being connected of heat conductive rod 13.By the heat build-up system heat is delivered on the heat conductive rod 13, body 1 is heated rapidly, produce 800-1500 ℃ of high temperature, waste water or seawater liquid film after falling within on this body 11 are heated rapidly, evaporate, the steam that is produced can be derived rapidly, be risen by gas port 12, introduce follow-up system, impurity or isolated salinity then fall behind down and form dry powder, reclaim or discharge by collection box 4.
Referring to Fig. 2, in the design of the utility model concrete structure, described heat-conducting plate 14 is connected with heating system 2, be fixedly set in described body 11 1 sides, each heat conductive rod 13 1 end is fixedly installed on the described heat-conducting plate 14, is arranged in parallel, and the other end extends in the described body 11.
Particularly, the thermostable heat-conductive material composition of described heat conductive rod 13 consists of: silicon nitride 80%-95% (weight percent); Two silicon nitride 5%-20% (weight percent) have very high heat conduction temperature tolerance, can reach the highest heat transfer intensification effect.
Further, in the utility model concrete structure design, or/and the below, also vertical row is shown a plurality of heating tubes 15 that are connected with heat conductive rod 13 in described heat conductive rod 13 tops.Described heating tube 15 can be that high temperature resistant silicon nitride thermally conductive material is made, and is provided with nichrome wire in heating tube 15, also can be metal tube, is provided with nichrome wire in heating tube 15.When adopting sun power heat build-up system to do heating system, sooner or later or the obnubilation gap relies on supplementary energy or energy stored is kept the whole wastewater treatment of system or seawater desalination system moves normally.
The above only is preferred embodiment of the present utility model; not in order to restriction the utility model; all any modifications of within spirit of the present utility model and principle, being done, be equal to and replace and improvement etc., all should be included within the protection domain of the present utility model.

Claims (5)

1. high temperature crystallization device, waste water or the seawater that is used for forming liquid film carries out the high temperature explosion, evaporative crystallization is handled, it is characterized in that: comprise a body, parallel rows is shown a plurality of gas ports as vapour passage in the described body, in the vertical direction of described gas port, be arranged with the heat conductive rod of many rows, the making of a plurality of thermostable heat-conductive material composition; Described heat conductive rod is connected with heater by a heat-conducting plate.
2. a kind of high temperature crystallization device as claimed in claim 1 is characterized in that: described heat-conducting plate is fixedly set in described body one side, and each heat conductive rod one end is loaded on the described heat-conducting plate, and the other end extends in the described body.
3. a kind of high temperature crystallization device as claimed in claim 1 or 2 is characterized in that: or/and the below, also vertical row is shown a plurality of heating tubes that are connected with heat conductive rod in described heat conductive rod top.
4. a kind of high temperature crystallization device as claimed in claim 3 is characterized in that: be provided with nichrome wire in the described heating tube.
5. a kind of high temperature crystallization device as claimed in claim 3, it is characterized in that: described heating tube is a metal tube, is provided with nichrome wire in it.
CN2010202208266U 2010-06-09 2010-06-09 High temperature crystallizer Expired - Lifetime CN201777904U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010202208266U CN201777904U (en) 2010-06-09 2010-06-09 High temperature crystallizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2010202208266U CN201777904U (en) 2010-06-09 2010-06-09 High temperature crystallizer

Publications (1)

Publication Number Publication Date
CN201777904U true CN201777904U (en) 2011-03-30

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CN2010202208266U Expired - Lifetime CN201777904U (en) 2010-06-09 2010-06-09 High temperature crystallizer

Country Status (1)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112387226A (en) * 2020-11-11 2021-02-23 润泰化学(泰兴)有限公司 Dealcoholization tower for producing isobutyl 2,2, 4-trimethyl-3-hydroxypentanoate

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112387226A (en) * 2020-11-11 2021-02-23 润泰化学(泰兴)有限公司 Dealcoholization tower for producing isobutyl 2,2, 4-trimethyl-3-hydroxypentanoate

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Granted publication date: 20110330