CN104841147A - Agitating type evaporator for salt-containing wastewater separation - Google Patents
Agitating type evaporator for salt-containing wastewater separation Download PDFInfo
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- CN104841147A CN104841147A CN201510260345.5A CN201510260345A CN104841147A CN 104841147 A CN104841147 A CN 104841147A CN 201510260345 A CN201510260345 A CN 201510260345A CN 104841147 A CN104841147 A CN 104841147A
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- tank body
- scraper plate
- stirring
- evaporimeter
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/138—Water desalination using renewable energy
- Y02A20/141—Wind power
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention discloses an agitating type evaporator for salt-containing wastewater separation. The agitating type evaporator for salt-containing wastewater separation comprises a tank body, a tank top and a tank bottom, wherein the tank body comprises a tank body upper portion connected with the tank top and a tank body lower portion connected with the tank bottom; the tank body is provided with a feed inlet, a discharge outlet, a gasification port and an agitating device; the tank bottom is provided with an inspection manhole; the tank body is further provided with a first scraping plate and a second scraping plate; the two scraping plates are provided with scraping plate through holes; a closed steam chamber is arranged between the two scraping plates; the steam chamber is provided with a steam inlet and a condensate outlet; a plurality of axially arranged evaporating tubes are provided in the steam chamber; the upper and lower ends of the evaporating tubes are respectively communicated with the scraping plate through holes in the first scraping plate and the second scraping plate; flow gaps are provided between the evaporating tubes; a backflow chamber is arranged between the second scraping plate and the tank bottom; the backflow chamber is communicated with the scraping plate through hole of the second scraping plate; the backflow chamber and the tank top are provided with thermometers; the agitating device comprises an agitating shaft, and the portion, at the tank bottom, of the agitating shaft is provided with agitating blades. The agitating type evaporator for salt-containing wastewater separation has the advantage of good evaporative separation effect.
Description
Technical field
The invention belongs to brine waste separation equipment technical field, be especially a kind ofly used for brine waste, to the stirring evaporimeter that wherein salinity is separated.
Background technology
For separating of the evaporating column of liquid mixture component in prior art, it isolates different liquid according to the boiling point different principle of liquid in different phase, the liquid reverse flow that the steam risen from evaporimeter and condenser flow out, there is heat trnasfer and matter transmission between the two, high boiling liquid moves to liquid from steam-condensation, low-boiling point liquid evaporates because of the condensation heat of release and is migrated in steam from liquid, and vapor enrichment low boiler cut, reaches separation object.Because evaporating column is that vertical stratification is arranged, usually have tens meters high, its volume is comparatively large, and inconvenient maintenance, and the filler in this evaporating column, easily cause tower body to block, cannot reach the object of separating liquid.In order to solve the problem, technical staff have developed a kind of scraper evaporator, its structure such as application publication number is " scraper evaporator " disclosed in the file of CN103861305A, it comprises the tank body of hollow, tank body top is provided with motor, rotating shaft is provided with in tank body, the output shaft of motor is connected with rotating shaft, the rotating shaft other end is provided with scraper plate, be provided with chuck outside tank body, tank body interior side-wall surface is provided with some reinforcements, and the rotating shaft between motor and scraper plate is provided with stirrer paddle, stirrer paddle vertically parallel interval is arranged, and tank body lower end is provided with holder.The rotating shaft that this evaporimeter drives scraper plate to rotate not easily is rocked.The present invention is the Curve guide impeller based on above-mentioned evaporimeter.
Summary of the invention
In order to overcome the deficiencies in the prior art, the invention provides a kind of stirring evaporimeter be separated for brine waste evaporating good separating effect, this evaporimeter volume is little, easy to process and be convenient to installation and repairing.
To achieve these goals, the technical solution used in the present invention is: a kind of stirring evaporimeter be separated for brine waste, comprise tank body, at the bottom of tank deck and tank, tank body comprises the tank body top be connected with tank deck, and with the tank body lower part be connected at the bottom of tank, it is characterized in that: tank body top is provided with charging aperture, tank body lower part and junction, top are provided with the first scraper plate, at the bottom of tank body lower part and tank, junction is provided with the second scraper plate, first scraper plate and the second scraper plate are equipped with scraper plate through hole, airtight vapor chamber is provided with between first scraper plate and the second scraper plate, vapor chamber offers steam inlet and the condensation mouth of a river, vapor chamber is provided with some evaporation tubes of axially-aligned, the upper and lower side of this evaporation tube is communicated with the scraper plate through hole on the second scraper plate with the first scraper plate respectively, having between evaporation tube and evaporation tube can for the flow gaps of vapor flow, also back cavity is provided with between at the bottom of this second scraper plate and tank, this back cavity is communicated with the scraper plate through hole of the second scraper plate, thermometer is equipped with tank deck in described back cavity, also agitating device is provided with in tank body, agitating device comprises by tank deck successively through the shaft extending to tank body lower part behind tank body top and the bottom, shaft is positioned at pot bottom and is arranged with stirrer paddle, discharging opening is provided with at the bottom of tank, maintenance population is also provided with at the bottom of tank, tank deck is also provided with vaporization mouth.
In said structure, material enters tank body from the charging aperture on tank body top, through the first scraper plate, evaporation tube, and second scraper plate, surrounding due to this evaporation tube has steam to carry out heating to the material entering this vapor chamber to make it be heated to become steam, the material of light boiling point continues to be separated by thermal evaporation by getting back to evaporation tube after the scraper plate through hole of the second scraper plate through back cavity, and discharge via the vaporization mouth on tank deck or tank body top, isolated heavy boiling component is discharged from the discharging opening at the bottom of tank after back cavity, obtain the salinity after being separated, this discharging opening can carry out according to the material component boiling point weight collected and be separately positioned on tank body top or pot bottom grades, the setting of above-mentioned agitating device causes for avoiding salinity to lump agglomerating in evaporation process the problem that cannot discharge, arranging of evaporation tube can carry out heating for multiple times separation to this material, make its separating effect better, and due to body arrange to backflow vapor composition there is barrier effect, slow down the speed that it rises, extend its time in pipe, further raising separating effect, in addition all having between evaporation tube and evaporation tube can for the space of steam circulation, every root pipe can be heated evenly, tank body lower part can also be provided with Pressure gauge and safety valve, moreover, above-mentioned tank body, tank deck, at the bottom of tank and evaporation tube and scraper plate etc. all have welding procedure one fixing, structure is simple, be convenient to processing.
Further, described first scraper plate and the second scraper plate all have centre bore, described vapor chamber structure ringwise, two centre bores and the vapor chamber inner hole wall of described first scraper plate and the second scraper plate form central passage, the upper and lower port of central passage is communicated with tank body top and back cavity respectively, and vapor chamber and central passage are isolated by vapor chamber inwall.
In said structure, evaporation tube is stainless steel tube, tank body is carbon steel material, sound construction, not perishable, durability is strong, above-mentioned vapor chamber is airtight loop configuration, steam wherein around its perisporium is capable take a round after discharge from another side lower end, this structure to prolong time of steam in vapor chamber, effectively utilize steam, moreover the outer wall of central passage is the inwall of annular chamber, therefore this central passage periphery is also filled with steam, this central passage in substance form the evaporation tube of larger caliber, therefore most of material from this central passage through out-of-date, evaporation separating effect can be improved, then, the vapor composition of backflow continues evaporation from tiny evaporation tube and is separated, improve separation purity, because material major part sweeps away through this central passage, steam in back cavity is difficult to owing to being subject to material impact reflux from this central passage, so the evaporation tube backflow in annular chamber can be turned to continue further to be separated, therefore the evaporimeter of this structure, evaporation tube after central passage initial gross separation again in annular chamber is purified further, its separating-purifying effect more, efficiency is better.
Further, described tank body top is also provided with observation window, and this observation window is distributed in both sides, tank body top and same level is coaxially arranged.
In said structure, this observation window can carry out monitoring to charging and steam situation of discharging to be observed, and is convenient to on-call maintenance.
Further, described tank body top is provided with the radial feed pipe extended, one end of this feed pipe is stretched out outside tank body and is formed described charging aperture, and the other end of feed pipe is arranged in tank body and extends to central passage place, and this end of feed pipe has and to bend towards central passage and to turn mouth to downward-extension.
In said structure, the mouth setting of turning of this feed pipe makes it corresponding with central passage, reduces the injection everywhere of material, makes material mainly enter tank body through central passage.
Further, described tank body lower part periphery is enclosed with insulation jacket, and this insulation jacket one end extends to tank body top, and the insulation jacket other end extends at the bottom of tank.
In said structure, the setting of insulation jacket, plays insulation effect to tank body, improves the utilization rate of steam.
Further, described insulation jacket is hollow structure, and this insulation jacket has the UNICOM's through hole be connected with described vapor chamber, and the described condensation mouth of a river is arranged on this insulation jacket and extends to one end at the bottom of tank.
The cavity of above-mentioned insulation jacket and vapor chamber UNICOM, steam in this vapor chamber enters insulation jacket and plays heat insulation effect to this tank body further after flow gaps rotates, the condensation mouth of a river again through being positioned at tank bottom is discharged, substantially prolongs the time of steam in tank body and insulation jacket, effectively can utilize steam thermal energy, reduce energy consumption.
Further, described tank body lower part periphery wall both sides are equipped with steam inlet, and steam inlet is arranged on one end that tank body lower part is connected with tank body top, and tapered structure at the bottom of described tank, discharging opening is arranged on the cone point at the bottom of tank.
In said structure, steam enters from the steam inlet of upper end and discharges from the condensation mouth of a river of lower end, tank body both sides are equipped with steam inlet, its circulating direction of the steam of both sides rushes mutually, when two strands of steam meet, be all obstructed, so the velocity of liquid assets of steam can be delayed, extend the currency of steam in vapor chamber, improve the effective rate of utilization of steam.Pyramidal structure at the bottom of tank, is convenient to the discharge of salinity.
Further, described stirrer paddle comprises the left and right blade parallel with cone point both sides inwall, respective one end of left and right blade is all fixed on shaft, the respective other end of left and right blade extends to form free end along inwall at the bottom of tank, affixed by a word blade between the respective free end of left and right blade, the center of this word blade is fixedly arranged on shaft, and the part that described shaft is positioned at tank body top is also provided with stirring vane.
In said structure, stirring vane and the tank Bottom Shape adaptation of pyramidal structure are convenient to stir, material is allowed to obtain better vaporizing faster, and the stirring of the stirrer paddle of this pyramidal structure can make material fast vaporizing, and prevent material crystallization on tank skin, moreover be connected to form well-set stirrer paddle by a word blade of upper end, the stirring vane on tank body top can play the heavier composition that certain barrier effect makes and fall after rise to the salinity up along steam.
Further, described tank deck is provided with protruding body, and have the passing away be communicated with vaporization mouth in this body, tube wall is provided with the interface be communicated with the port of export of passing away, is provided with stop step surface in passing away.
In said structure, the stop step surface in this passing away has barrier effect for the salinity risen with steam, avoids it together to discharge with steam, plays further separating-purifying effect.
Further, described tank deck is also provided with overhaul reserve mouth, and overhaul reserve mouth is separately positioned at the bottom of tank deck and tank with maintenance population, and overhaul reserve mouth and vaporization mouth lay respectively at tank deck both sides, and one end that shaft stretches out tank deck is connected with fire-proof motor.
In said structure, maintenance population is positioned at below easy access pot bottom and divides, and avoid discharging opening block and cause problem of cannot discharging, overhaul reserve mouth is positioned at the maintenance that tank body top is then convenient in upper end.
Adopt such scheme, structure of the present invention is simple, be convenient to processing, separating-purifying is effective, steam utilization is high.
Below in conjunction with accompanying drawing, the invention will be further described.
Accompanying drawing explanation
Accompanying drawing 1 is specific embodiment of the invention structural representation;
Accompanying drawing 2 is specific embodiment of the invention structure top view;
Accompanying drawing 3 is the structural representation of the specific embodiment of the invention first scraper plate and the second scraper plate;
Accompanying drawing 4 is the enlarged drawing of local A in specific embodiment of the invention accompanying drawing 1;
Accompanying drawing 5 is the enlarged drawing of local B in specific embodiment of the invention accompanying drawing 1;
Tank body top 11, tank body lower part 12, tank deck 2, body 21, passing away 211, stop step surface 212, interface 213, at the bottom of tank 3, first scraper plate 41, second scraper plate 42, scraper plate through hole 431, centre bore 432, vapor chamber 5, flow gaps 51, central passage 52, evaporation tube 6, back cavity 7, shaft 81, lobus sinister sheet 82, lobus dexter sheet 83, one word blade 84, stirring vane 85, fire-proof motor 86, charging baffle plate 87, insulation jacket 9, feed pipe N1, charging aperture N2, steam inlet N3, condensation mouth of a river N4, vaporization mouth N4', discharging opening N5, maintenance population M2, overhaul reserve mouth M1, observation window E.
Detailed description of the invention
Specific embodiments of the invention are the stirring evaporimeter be separated for brine waste as Figure 1-5, comprise tank body, at the bottom of tank deck 2 and tank 3, tank body comprises the tank body top 11 be connected with tank deck 2, and with 3 tank body lower parts be connected 12 at the bottom of tank, tank body top 11 is provided with charging aperture N2, tank body lower part 12 and junction, top are provided with the first scraper plate 41, tank body lower part 12 is provided with the second scraper plate 42 with 3 junctions at the bottom of tank, first scraper plate 41 and the second scraper plate 42 are equipped with scraper plate through hole 431, airtight vapor chamber 5 is provided with between first scraper plate 41 and the second scraper plate 42, vapor chamber 5 offers steam inlet N3 and condensation mouth of a river N4, vapor chamber 5 is provided with some evaporation tubes 6 of axially-aligned, the upper and lower side of this evaporation tube 6 is communicated with the scraper plate through hole 431 on the second scraper plate 42 with the first scraper plate 41 respectively, having between evaporation tube 6 and evaporation tube 6 can for the flow gaps 51 of vapor flow, back cavity 7 is also provided with between 3 at the bottom of this second scraper plate 42 and tank, this back cavity 7 is communicated with the scraper plate through hole 431 of the second scraper plate 42, thermometer is equipped with tank deck 2 in back cavity 7, also agitating device is provided with in tank body, agitating device comprises by tank deck 2 successively through tank body top and the bottom 11, the shaft 81 of tank body lower part 12 is extended to after 12, shaft 81 is positioned at 3 parts at the bottom of tank and is provided with stirrer paddle, at the bottom of tank, 3 are provided with discharging opening N5, tank body top 11 is also provided with maintenance population M2 and vaporization mouth N4'.
Above-mentioned first scraper plate 41 and the second scraper plate 42 all have centre bore 432, vapor chamber 5 structure ringwise, two centre bores 432 and vapor chamber 5 inner hole wall of the first scraper plate 41 and the second scraper plate 42 form central passage 52, the upper and lower port of central passage 52 is communicated with tank body top 11 and back cavity 7 respectively, and vapor chamber 5 is isolated by vapor chamber 5 inwall with central passage 52.
Above-mentioned shaft 81 is positioned at 3 parts at the bottom of tank and is provided with for stopping that the raw material fallen by central passage 52 directly enters the charging baffle plate 87 of at the bottom of tank 3, this charging baffle plate 87 is positioned at below central passage 52, stop is played to the raw material entered by feed pipe N1, it is avoided directly to pour at the bottom of tank 3, mix with the heavy boiling component through being separated, interference is caused to separation.
Above-mentioned tank body top 11 is also provided with observation window E, and this observation window E is distributed in both sides, tank body top 11 and same level is coaxially arranged.
Above-mentioned tank body top 11 is provided with the radial feed pipe N1 extended, one end of this feed pipe N1 is stretched out outside tank body and is formed charging aperture N2, the other end of feed pipe N1 is arranged in tank body and extends to central passage 52 place, and this end of feed pipe N1 has towards central passage 52 bending and turn mouth to downward-extension.
Above-mentioned tank body lower part 12 periphery is enclosed with insulation jacket 9, and this insulation jacket 9 one end extends to tank body top 11, and insulation jacket 9 other end to extend at the bottom of tank 12.
This insulation jacket 9 is hollow structure, and this insulation jacket 9 has the UNICOM's through hole be connected with vapor chamber 5, and condensation mouth of a river N4 is arranged on one end that this insulation jacket 9 extends at the bottom of tank 3.
Above-mentioned tank body lower part 12 periphery wall both sides are equipped with steam inlet N3, and steam inlet N3 is arranged on one end that tank body lower part 12 is connected with tank body top 11.
3 tapered structures at the bottom of above-mentioned tank, discharging opening N5 is arranged on the cone point of at the bottom of tank 3.
Above-mentioned stirrer paddle comprises the left and right blade 82,83 parallel with cone point both sides inwall, respective one end of left and right blade 82,83 is all fixed on shaft 81, the respective other end 3 inwalls at the bottom of tank of left and right blade 82,83 extend to form free end, affixed by a word blade 84 between the respective free end of left and right blade 82,83, the center of this word blade 84 is fixedly arranged on shaft 81, this word blade also plays the effect accelerated material and better vaporize sooner, and the part that shaft 81 is positioned at tank body top 11 is also provided with stirring vane 85.
Above-mentioned tank deck 2 is provided with protruding body 21, and have the passing away 211 be communicated with vaporization mouth N4' in this body 21, body 21 sidewall is provided with the interface 213 be communicated with the port of export of passing away 211, is provided with and stops step surface 212 in passing away 211.
Above-mentioned tank deck 2 is also provided with overhaul reserve mouth M1, overhaul reserve mouth M1 and maintenance population M2 to be separately positioned at the bottom of tank deck 2 and tank 3, overhaul reserve mouth M1 and the mouth N4' that vaporizes lay respectively at tank deck 2 both sides, one end that shaft 81 stretches out tank deck 2 is connected with fire-proof motor 86.
Structure of the present invention is simple, be convenient to processing, separating-purifying is effective, steam utilization is high.The present invention is not limited to above-mentioned detailed description of the invention; persons skilled in the art are according to content disclosed by the invention; other multiple detailed description of the invention can be adopted to implement of the present invention; or every employing project organization of the present invention and thinking; do simple change or change, all fall into protection scope of the present invention.
Claims (10)
1. the stirring evaporimeter be separated for brine waste, comprise tank body, at the bottom of tank deck and tank, tank body comprises the tank body top be connected with tank deck, and with the tank body lower part be connected at the bottom of tank, it is characterized in that: tank body top is provided with charging aperture, tank body lower part and junction, top are provided with the first scraper plate, at the bottom of tank body lower part and tank, junction is provided with the second scraper plate, first scraper plate and the second scraper plate are equipped with scraper plate through hole, airtight vapor chamber is provided with between first scraper plate and the second scraper plate, vapor chamber offers steam inlet and the condensation mouth of a river, vapor chamber is provided with some evaporation tubes of axially-aligned, the upper and lower side of this evaporation tube is communicated with the scraper plate through hole on the second scraper plate with the first scraper plate respectively, having between evaporation tube and evaporation tube can for the flow gaps of vapor flow, also back cavity is provided with between at the bottom of this second scraper plate and tank, this back cavity is communicated with the scraper plate through hole of the second scraper plate, thermometer is equipped with tank deck in described back cavity, also agitating device is provided with in tank body, agitating device comprises by tank deck successively through the shaft extending to tank body lower part behind tank body top and the bottom, shaft is positioned at pot bottom and is arranged with stirrer paddle, discharging opening is provided with at the bottom of tank, maintenance population is also provided with at the bottom of tank, tank deck is also provided with vaporization mouth.
2. the stirring evaporimeter be separated for brine waste according to claim 1, it is characterized in that: described first scraper plate and the second scraper plate all have centre bore, described vapor chamber structure ringwise, two centre bores and the vapor chamber inner hole wall of described first scraper plate and the second scraper plate form central passage, the upper and lower port of central passage is communicated with tank body top and back cavity respectively, and vapor chamber and central passage are isolated by vapor chamber inwall.
3. the stirring evaporimeter be separated for brine waste according to claim 2, it is characterized in that: described tank body top is also provided with observation window, this observation window is distributed in both sides, tank body top and same level is coaxially arranged.
4. the stirring evaporimeter be separated for brine waste according to claim 2, it is characterized in that: described tank body top is provided with the radial feed pipe extended, one end of this feed pipe is stretched out outside tank body and is formed described charging aperture, the other end of feed pipe is arranged in tank body and extends to central passage place, and this end of feed pipe has and to bend towards central passage and to turn mouth to downward-extension.
5. the stirring evaporimeter be separated for brine waste according to claim 1 or 2 or 3 or 4, it is characterized in that: described tank body lower part periphery is enclosed with insulation jacket, this insulation jacket one end extends to tank body top, and the insulation jacket other end extends at the bottom of tank.
6. the stirring evaporimeter be separated for brine waste according to claim 5, it is characterized in that: described insulation jacket is hollow structure, this insulation jacket has the UNICOM's through hole be connected with described vapor chamber, and the described condensation mouth of a river is arranged on this insulation jacket and extends to one end at the bottom of tank.
7. the stirring evaporimeter be separated for brine waste according to claim 1, it is characterized in that: described tank body lower part periphery wall both sides are equipped with steam inlet, and steam inlet is arranged on one end that tank body lower part is connected with tank body top, tapered structure at the bottom of described tank, discharging opening is arranged on the cone point at the bottom of tank.
8. the stirring evaporimeter be separated for brine waste according to claim 7, it is characterized in that: described stirrer paddle comprises the left and right blade parallel with cone point both sides inwall, respective one end of left and right blade is all fixed on shaft, the respective other end of left and right blade extends to form free end along inwall at the bottom of tank, affixed by a word blade between the respective free end of left and right blade, the center of this word blade is fixedly arranged on shaft, and the part that described shaft is positioned at tank body top is also provided with stirring vane.
9. the stirring evaporimeter be separated for brine waste according to claim 1, it is characterized in that: described tank deck is provided with protruding body, there is in this body the passing away be communicated with vaporization mouth, tube wall is provided with the interface be communicated with the port of export of passing away, is provided with stop step surface in passing away.
10. the stirring evaporimeter be separated for brine waste according to claim 1, it is characterized in that: described tank deck is also provided with overhaul reserve mouth, overhaul reserve mouth is separately positioned at the bottom of tank deck and tank with maintenance population, overhaul reserve mouth and vaporization mouth lay respectively at tank deck both sides, and one end that shaft stretches out tank deck is connected with fire-proof motor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510260345.5A CN104841147A (en) | 2015-05-20 | 2015-05-20 | Agitating type evaporator for salt-containing wastewater separation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510260345.5A CN104841147A (en) | 2015-05-20 | 2015-05-20 | Agitating type evaporator for salt-containing wastewater separation |
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| Publication Number | Publication Date |
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| CN104841147A true CN104841147A (en) | 2015-08-19 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510260345.5A Pending CN104841147A (en) | 2015-05-20 | 2015-05-20 | Agitating type evaporator for salt-containing wastewater separation |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106422383A (en) * | 2016-10-10 | 2017-02-22 | 肇庆市和邦机械制造有限公司 | Short-range evaporator |
| CN107051309A (en) * | 2017-04-28 | 2017-08-18 | 上海数郜机电有限公司 | One kind shearing scraper-type Vacuum Mixture tank |
| CN107982944A (en) * | 2017-12-28 | 2018-05-04 | 天津普恒康泰科技有限公司 | A kind of evaporated crystallization device for preventing discharge blockage, efficiently turning heat |
| CN108392090A (en) * | 2018-05-25 | 2018-08-14 | 广东美的厨房电器制造有限公司 | Steam generator and steam cooking apparatus |
| CN109734234A (en) * | 2019-02-22 | 2019-05-10 | 江苏和顺环保有限公司 | A kind of processing unit of copper-containing wastewater |
| CN110410804A (en) * | 2019-07-09 | 2019-11-05 | 四川明月环保科技有限公司 | A kind of organic wastewater atomization incinerator and incinerating method |
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| CN2146289Y (en) * | 1993-02-20 | 1993-11-17 | 邓跃敏 | Vacuum evaporation crystallizer |
| CN101185811A (en) * | 2007-09-13 | 2008-05-28 | 天津渤天化工有限责任公司 | Exhalation heat exchanger |
| CN103331025A (en) * | 2013-06-18 | 2013-10-02 | 天津科技大学 | Ultrasonic evaporator |
| CN204093065U (en) * | 2014-09-02 | 2015-01-14 | 武汉金榜轻工机械设备有限公司 | A kind of single-action scraper concentrator |
| CN204107070U (en) * | 2014-09-27 | 2015-01-21 | 武汉金榜轻工机械设备有限公司 | A kind of scraper concentrator |
| CN204815718U (en) * | 2015-05-20 | 2015-12-02 | 浙江创兴化工设备有限公司 | A stirring evaporimeter for containing separation of salt waste water |
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| CN2146289Y (en) * | 1993-02-20 | 1993-11-17 | 邓跃敏 | Vacuum evaporation crystallizer |
| CN101185811A (en) * | 2007-09-13 | 2008-05-28 | 天津渤天化工有限责任公司 | Exhalation heat exchanger |
| CN103331025A (en) * | 2013-06-18 | 2013-10-02 | 天津科技大学 | Ultrasonic evaporator |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106422383A (en) * | 2016-10-10 | 2017-02-22 | 肇庆市和邦机械制造有限公司 | Short-range evaporator |
| CN107051309A (en) * | 2017-04-28 | 2017-08-18 | 上海数郜机电有限公司 | One kind shearing scraper-type Vacuum Mixture tank |
| CN107982944A (en) * | 2017-12-28 | 2018-05-04 | 天津普恒康泰科技有限公司 | A kind of evaporated crystallization device for preventing discharge blockage, efficiently turning heat |
| CN108392090A (en) * | 2018-05-25 | 2018-08-14 | 广东美的厨房电器制造有限公司 | Steam generator and steam cooking apparatus |
| CN108392090B (en) * | 2018-05-25 | 2023-12-08 | 广东美的厨房电器制造有限公司 | Steam generator and steam cooking device |
| CN109734234A (en) * | 2019-02-22 | 2019-05-10 | 江苏和顺环保有限公司 | A kind of processing unit of copper-containing wastewater |
| CN110410804A (en) * | 2019-07-09 | 2019-11-05 | 四川明月环保科技有限公司 | A kind of organic wastewater atomization incinerator and incinerating method |
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Application publication date: 20150819 |