CN105129890A - Evaporating crystallizer - Google Patents
Evaporating crystallizer Download PDFInfo
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- CN105129890A CN105129890A CN201510637882.7A CN201510637882A CN105129890A CN 105129890 A CN105129890 A CN 105129890A CN 201510637882 A CN201510637882 A CN 201510637882A CN 105129890 A CN105129890 A CN 105129890A
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- salt
- evaporator room
- heat exchanger
- circulation tube
- outlet
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- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
An evaporating crystallizer comprises an evaporating chamber, a heat exchanger, a forced circulating pump, a circulating pipe clamp sleeve and a salt leg. A foam remover is arranged in the evaporating chamber. Spraying devices are arranged in front of and behind the foam remover. A horn mouth is formed in the center of the foam remover and is located below the liquid level. The forced circulating pump is connected with the heat exchanger through a circulating pipe in a side-inlet and top-outlet mode. A material liquid inlet is formed in the horizontal section of the circulating pipe. A clamp sleeve connector is arranged on the perpendicular section of the circulating pipe. By means of forced circulating heat exchange, the possibility that salt-bearing wastewater is prone to blocking the heat exchanger and producing scales in the heat exchanger in a conventional process is lowered; meanwhile, by means of the built-in foam remover and the spraying devices, secondary steam carries little liquid foam; due to the tank type, the evaporating crystallizer is suitable for various salt-bearing wastewater concentration working conditions, is particularly suitable for an MVR process device, can achieve continuous production, and is long in running cycle, stable in operation and convenient to control.
Description
Technical field
The invention belongs to sewage treatment equipment, particularly relate to the evaporative crystallizer for industry process waste water such as pulping and paper-making, Coal Chemical Industry, desulfurization wastewaters.
Background technology
In the brine waste treatment process in the fields such as pulping and paper-making, Coal Chemical Industry, desulfurization wastewater, most of water can be reclaimed by techniques such as pre-treatment, ultrafiltration+reverse osmosis, nanofiltration, electrodialysis, but inevitably produce a part of high-concentration salt-containing wastewater.Containing the inorganic salt such as a large amount of sodium-chlor and sodium sulfate in these high dense brine wastes, if do not processed directly outer row, not only can cause the significant wastage of resource, also can cause the pollution of local environment.The brine waste evaporation treatment process of current routine, the vaporizer of employing has plate-type evaporator, falling-film evaporator, climbing-film evaporator.This type of vaporizer applicable elements is harsher, is all not too applicable to the operating mode easily producing crystallization, easy occluding device, and cause brush tank frequent, the production cycle shortens, and before impact, operation is produced.
Summary of the invention
The object of the present invention is to provide a kind of evaporative crystallizer, be applicable to the brine waste evaporation process under multiple concentration, mixture condition, equipment, the blocking of heat transfer tube, fouling and the frequent brush tank, the cleaning problem that cause can be solved.
The technical scheme of invention:
Evaporative crystallizer, comprise evaporator room, heating chamber, forced circulation pump, circulation tube, salt leg, evaporator room top cone section is provided with venting port, observation visor, scum dredger, spray equipment, secondary steam outlet, evaporator room top is provided with venting port, evaporation chamber is provided with hydraucone, and hydraucone is below liquid level; The top of heating chamber is provided with steam inlet, and bottom is provided with condensation-water drain, and upper and lower two ends are provided with non-condensable gas outlet; The mode that forced circulation pump adopts side to enter to eject is connected with interchanger by circulation tube; Circulation tube vertical section is provided with chuck, and chuck arranges mother liquor outlet, and circulation tube horizontal section is provided with brine waste import, discharging hole, thief hole; Salt leg is connected with bottom evaporator room, is provided with the outlet of salt slurry, evacuation port, elutriation mouth, observes visor below salt leg.
The present invention has following beneficial effect: compared with traditional same category of device, and this evaporative crystallizer is forced circulation evaporation crystallizer.Be the pump circulation heat exchange of large discharge due to what adopt, decrease that brine waste in Conventional vaporizer easily blocks in interchanger, the probability of fouling; Adopt in chuck and discharge the foreign ion balance that a small amount of mother liquor can ensure evaporative crystallizer system, the long-term stability maintaining system is run; Salt leg adopts the mode eluriated simultaneously, maintains disturbance bottom salt leg, ensures the continuous discharge of slurry, can realize continuous seepage, and the equipment cycle of operation extends, and stable operation is convenient to control.
Accompanying drawing explanation
Fig. 1 is invention structural representation.
In figure: 1-evaporator room, 2-heating chamber, 3-forced circulation pump, 4-circulation tube, 5-salt leg, 6-venting port, 7-observes visor, 8-scum dredger, 9-spray equipment, 10-secondary steam exports, 11-hydraucone, 12-steam inlet, 13-condensation-water drain, 14-non-condensable gas exports, 15-mother liquor outlet, the import of 16-brine waste, 17-discharging hole, 18-thief hole, the outlet of 19-salt slurry, 20-evacuation port, 21-eluriates mouth, and 22-observes visor, 23-chuck.
Embodiment
Below in conjunction with accompanying drawing embodiment, the present invention is further elaborated.
As shown in Figure 1, evaporative crystallizer comprises evaporator room 1, heating chamber 2, forced circulation pump 3, circulation tube 4, salt leg 5, evaporator room top cone section is provided with venting port 6, observation visor 7, scum dredger 8, spray equipment 9, secondary steam outlet 10, evaporator room 1 top is provided with venting port 6, and evaporator room 1 inside is provided with hydraucone 11, and hydraucone 11 is below liquid level; The top of heating chamber is provided with steam inlet 12, and bottom is provided with condensation-water drain 13, and upper and lower two ends are provided with non-condensable gas outlet 14; The mode that forced circulation pump 3 adopts side to enter to eject is connected with interchanger by circulation tube; Circulation tube 4 vertical section is provided with chuck 23, chuck is arranged mother liquor outlet 15, and circulation tube 4 horizontal section is provided with brine waste import 16, discharging hole 17, thief hole 18; Salt leg 5 is connected with bottom evaporator room 1, is provided with the outlet 19 of salt slurry, evacuation port 20, eluriates mouth 21, observes visor 22 below salt leg 5.
The present invention is applied in the evaporative crystallization technique of brine waste, specific operation process is as follows: by brine waste by entering circulation tube 4 entrance of evaporative crystallizer after preheater preheats, contact with a large amount of high temperature circulation feed liquid in circulation tube 4, under the drive of forced circulation pump, enter heating chamber 2 together carry out heat exchange, control the internal-external temperature difference of heat transfer tube and the internal circulating load of feed liquid, the plugging phenomenon in circulation feed liquid heat transfer process can be avoided to occur.Feed liquid after heat exchange is by circulation tube 4 hydraucone 11 in crystallisation chamber evaporation concentration, and the secondary steam evaporated enters vapour compressor, and the superheated vapour of the high enthalpy of compressed formation, delivers to heating chamber after spray desuperheating to saturation steam and recycle.Crystallize out after feed liquid reaches capacity in evaporator room, macrobead solid falls into salt leg 5 in settling process, head into raw material brine waste at salt leg 5, ensure that salt slurry is expelled to solid-liquid separation process smoothly from salt leg 5, a small amount of concentrated mother liquor is discharged by chuck mother liquor outlet simultaneously.
Claims (1)
1. evaporative crystallizer, it is characterized in that: comprise evaporator room 1, heating chamber 2, forced circulation pump 3, circulation tube 4, salt leg 5, evaporator room top cone section is provided with venting port 6, observation visor 7, scum dredger 8, spray equipment 9, secondary steam outlet 10, evaporator room 1 top is provided with venting port 6, and evaporator room 1 inside is provided with hydraucone 11, and hydraucone 11 is below liquid level; The top of heating chamber is provided with steam inlet 12, and bottom is provided with condensation-water drain 13, and upper and lower two ends are provided with non-condensable gas outlet 14; The mode that forced circulation pump 3 adopts side to enter to eject is connected with interchanger by circulation tube; Circulation tube 4 vertical section is provided with chuck 23, chuck is arranged mother liquor outlet 15, and circulation tube 4 horizontal section is provided with brine waste import 16, discharging hole 17, thief hole 18; Salt leg 5 is connected with bottom evaporator room 1, is provided with the outlet 19 of salt slurry, evacuation port 20, eluriates mouth 21, observes visor 22 below salt leg 5.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201510637882.7A CN105129890A (en) | 2015-10-07 | 2015-10-07 | Evaporating crystallizer |
Applications Claiming Priority (1)
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CN201510637882.7A CN105129890A (en) | 2015-10-07 | 2015-10-07 | Evaporating crystallizer |
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CN105129890A true CN105129890A (en) | 2015-12-09 |
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CN201510637882.7A Pending CN105129890A (en) | 2015-10-07 | 2015-10-07 | Evaporating crystallizer |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106395949A (en) * | 2016-11-30 | 2017-02-15 | 江苏迈安德节能蒸发设备有限公司 | Treatment system of sodium sulfate wastewater |
CN108191130A (en) * | 2017-12-28 | 2018-06-22 | 北京国电富通科技发展有限责任公司 | A kind of high organic wastewater evaporative crystallization antiscaling treatment method with high salt and device |
CN109481952A (en) * | 2018-11-28 | 2019-03-19 | 江苏瑞升华能源科技有限公司 | A kind of MVR crystallizes out salt crystal grain control system and control method |
CN110028121A (en) * | 2019-05-10 | 2019-07-19 | 成都三顶环保科技有限公司 | Desulfurization wastewater treatment system |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007275821A (en) * | 2006-04-10 | 2007-10-25 | Sasakura Engineering Co Ltd | Evaporation concentrator for aqueous solution |
CN201101905Y (en) * | 2007-09-28 | 2008-08-20 | 项文远 | Continuous evaporation crystallizer |
CN103071310A (en) * | 2013-01-31 | 2013-05-01 | 江苏井神盐化股份有限公司 | Evaporating crystallizer |
-
2015
- 2015-10-07 CN CN201510637882.7A patent/CN105129890A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007275821A (en) * | 2006-04-10 | 2007-10-25 | Sasakura Engineering Co Ltd | Evaporation concentrator for aqueous solution |
CN201101905Y (en) * | 2007-09-28 | 2008-08-20 | 项文远 | Continuous evaporation crystallizer |
CN103071310A (en) * | 2013-01-31 | 2013-05-01 | 江苏井神盐化股份有限公司 | Evaporating crystallizer |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106395949A (en) * | 2016-11-30 | 2017-02-15 | 江苏迈安德节能蒸发设备有限公司 | Treatment system of sodium sulfate wastewater |
CN108191130A (en) * | 2017-12-28 | 2018-06-22 | 北京国电富通科技发展有限责任公司 | A kind of high organic wastewater evaporative crystallization antiscaling treatment method with high salt and device |
CN108191130B (en) * | 2017-12-28 | 2020-11-10 | 北京国电富通科技发展有限责任公司 | High-salt high-organic matter wastewater evaporative crystallization anti-scaling treatment device and method |
CN109481952A (en) * | 2018-11-28 | 2019-03-19 | 江苏瑞升华能源科技有限公司 | A kind of MVR crystallizes out salt crystal grain control system and control method |
CN109481952B (en) * | 2018-11-28 | 2024-05-10 | 江苏瑞升华能源科技有限公司 | MVR crystallization salt crystal grain control system and control method |
CN110028121A (en) * | 2019-05-10 | 2019-07-19 | 成都三顶环保科技有限公司 | Desulfurization wastewater treatment system |
CN110028121B (en) * | 2019-05-10 | 2021-10-22 | 成都三顶环保科技有限公司 | Desulfurization wastewater treatment system |
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Application publication date: 20151209 |
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