CN204454673U - Be applicable to the MVR evaporative crystallizer of saliferous containing the crystallization of organism Waste water concentrating - Google Patents
Be applicable to the MVR evaporative crystallizer of saliferous containing the crystallization of organism Waste water concentrating Download PDFInfo
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- CN204454673U CN204454673U CN201420872892.XU CN201420872892U CN204454673U CN 204454673 U CN204454673 U CN 204454673U CN 201420872892 U CN201420872892 U CN 201420872892U CN 204454673 U CN204454673 U CN 204454673U
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Abstract
The utility model relates to saliferous in every profession and trade and contains the technical field of organism wastewater treatment, be applicable to the MVR evaporative crystallizer of saliferous containing the crystallization of organism Waste water concentrating, comprise effect body, effect body comprises vaporizer body, and vaporizer body comprises well heater, separate chamber or crystallisation chamber; Effect body has five, the first effect body, the second effect body composition double-effect evaporator, and triple effect body is single-effect evaporator, and quadruple effect body is single-effect evaporation crystallizer, and the 5th effect body is single-effect evaporation crystallizer; Separate chamber's outlet of the first effect body is connected with the second heat ingress of imitating the well heater of body, second and third, four, five effect the separate chambers of body or the outlet of crystallisation chamber be connected with a mechanical compressor import, mechanical compressor outlet be connected with first and third, four, five heat ingress of imitating the well heater of body.When the utility model runs, different operation working conditions be have employed to the concentration and evaporation of the waste water that different concns and different boiling rise and crystallization.
Description
Technical field
The utility model relates to saliferous in every profession and trade and, containing the technical field of organism wastewater treatment, is specifically related to a kind of to the evaporative crystallizer of saliferous containing the crystallization of organism Waste water concentrating.
Background technology
Saliferous is will be heated to boiling state containing inorganic salt and organic waste water by the mode of heat exchange containing the evaporating, concentrating and crystallizing of organic wastewater, the water of the overwhelming majority can be made to be vaporized be separated and the recycling that is condensed, the inorganic salt concentration evaporated in the waste water of large water gaging is improved until inorganic salt crystallization also can be recovered utilization.
Traditional evaporating, concentrating and crystallizing is the process of a highly energy-consuming, MVR evaporating, concentrating and crystallizing device be developed use achieve heat energy almost can whole recycling utilization, thus evaporating, concentrating and crystallizing can be made to be no longer traditional highly energy-consuming process, but for saliferous containing the crystallization of organism Waste water concentrating MVR evaporating, concentrating and crystallizing flow process configuration whether can meet wastewater treatment requirement, can make again the investment running cost of equipment all lower be to MVR evaporating, concentrating and crystallizing for saliferous containing organism wastewater treatment propose higher requirement.
Utility model content
The purpose of this utility model is, provides a kind of and may be used for being applicable to the MVR evaporative crystallizer of saliferous containing the crystallization of organism Waste water concentrating, to solve the problems of the technologies described above.
The technical problem that the utility model solves can realize by the following technical solutions:
Be applicable to the MVR evaporative crystallizer of saliferous containing the crystallization of organism Waste water concentrating, comprise effect body, described effect body comprises vaporizer body, and described vaporizer body comprises well heater, the separate chamber be connected with described well heater or crystallisation chamber; It is characterized in that, effect body has five, comprising the first effect body, the second effect body that rise all also lower waste water evaporation concentration for concentration and boiling point, and described first effect body, the second effect body composition double-effect evaporator; Also comprise the triple effect body of the evaporation concentration of the waste water risen for higher concentration and boiling point, described triple effect body is single-effect evaporator; Also comprise the quadruple effect body of the evaporation concentration of the waste water risen for greater concn and boiling point, described quadruple effect body is single-effect evaporation crystallizer; Also comprise the 5th effect body of the evaporation concentration of the waste water risen for very high density and boiling point, described 5th effect body is single-effect evaporation crystallizer;
Separate chamber's outlet of described first effect body is connected with the described second heat ingress of imitating the well heater of body, the secondary steam of described first effect evacuator body enters the well heater of the second effect body as heat source, water of condensation after described heat source completes heat exchange is collected to condensate water pot, described second, three, four, the five effect separate chambers of body or the outlet of crystallisation chamber are connected with a mechanical compressor import, described mechanical compressor outlet is with described first, three, four, the heat ingress of the well heater of five effect bodies is connected, described second, three, four, the water vapor of five effect evacuator bodies heats rear feeding first by mechanical compressor supercharging, three, four, the well heater of five effect bodies is as heat source, discharged by pump after water of condensation after described heat source completes heat exchange is collected to condensate water pot.
The utility model concentrates owing to have employed MVR (mechanically compress) double-effect evaporation+and single-effect evaporation concentrates+mode of the condensing crystal of dual evaporation crystallizer, different operation working conditions be have employed to the concentration and evaporation of the waste water that different concns and different boiling rise and crystallization during operation, the wastewater treatment that saliferous can be made to contain the crystallization of organism Waste water concentrating can accomplish recycling close to whole of water source effectively, inorganic salt also can be recycled close to whole crystallization, it is little that treatment capacity arranged outward by high dense organic concentrated solution, in turn ensure that simultaneously and can adopt MVR evaporation technique and the abundant recycling utilization that can reach heat energy, saliferous can be made to contain the wastewater treatment of organism Waste water concentrating crystallization can in safety, energy-conservation, environmental protection, efficient evaporating, concentrating and crystallizing technology gets off to complete.
Be applicable to saliferous containing the crystallization of organism Waste water concentrating MVR evaporative crystallizer described second and third, four, the outlets of intermediate water steam of five effect evacuator bodies are provided with a mechanical compressor, can return after heating for evaporated secondary steam supercharging described first and third, four, five effect bodies as heating steam, achieve heat energy close to 100% recycling utilization.
Be applicable to saliferous and be furnished with condensation water collection tank and condensate water discharge pump containing the water of condensation in the well heater of five effect bodies of the MVR evaporative crystallizer of organism Waste water concentrating crystallization, the collection of water of condensation can be ensured and recycle.
Be applicable to the opening for feed that saliferous imitates evacuator body device containing the MVR evaporative crystallizer first of organism Waste water concentrating crystallization and be provided with a feed rate Controlling System, described feed rate Controlling System comprises a liquid level sensor and a pneumatic adjusting valve, the open degree of described pneumatic adjusting valve presses the level value auto-adjustment control of described liquid level sensor setting, the set(ting)value of described liquid level sensor imitates the necessary level set of evacuator body device by described first, be applicable to saliferous and be connected with a set of electrical control cabinet containing the MVR evaporative crystallizer of organism Waste water concentrating crystallization, the Controlling System of described pneumatic adjusting valve and liquid level sensor and electrical control cabinet forms charging automatic control system, described feeding control system, the control end of automatic train control system is positioned at described housing, described housing is provided with the communication connection of Ethernet interface for same master control room.
Be applicable to the opening for feed that saliferous imitates evacuator body device containing the MVR evaporative crystallizer second of organism Waste water concentrating crystallization and be provided with a feed rate Controlling System, described feed rate Controlling System comprises a liquid level sensor and a pneumatic adjusting valve, the open degree of described pneumatic adjusting valve presses the level value auto-adjustment control of described liquid level sensor setting, the set(ting)value of described liquid level sensor imitates the necessary level set of evacuator body device by described second, the described saliferous that is applicable to is connected with a set of electrical control cabinet containing the MVR evaporative crystallizer of organism Waste water concentrating crystallization, the Controlling System of described pneumatic adjusting valve and liquid level sensor and electrical control cabinet forms charging automatic control system, described feeding control system, the control end of automatic train control system is positioned at described housing, described housing is provided with the communication connection of Ethernet interface for same master control room.
Be applicable to saliferous and be provided with two cover incoming flow amount control systems containing the opening for feed of MVR evaporative crystallizer triple effect evacuator body device of organism Waste water concentrating crystallization, described feed rate Controlling System comprises two liquid level sensors and two pneumatic adjusting valves, the open degree of described pneumatic adjusting valve presses the level value auto-adjustment control of described liquid level sensor setting, the set(ting)value of described liquid level sensor presses the necessary level set of described triple effect evacuator body device, the described saliferous that is applicable to is connected with a set of electrical control cabinet containing the MVR evaporative crystallizer of organism Waste water concentrating crystallization, the Controlling System of described pneumatic adjusting valve and liquid level sensor and electrical control cabinet forms charging automatic control system, described feeding control system, the control end of automatic train control system is positioned at described housing, described housing is provided with the communication connection of Ethernet interface for same master control room.
Be applicable to saliferous and be provided with a feed rate Controlling System containing the opening for feed of MVR evaporative crystallizer quadruple effect evacuator body device of organism Waste water concentrating crystallization, described feed rate Controlling System comprises a liquid level sensor and a pneumatic adjusting valve, the open degree of described pneumatic adjusting valve presses the level value auto-adjustment control of described liquid level sensor setting, the set(ting)value of described liquid level sensor presses the necessary level set of described quadruple effect evacuator body device, the described saliferous that is applicable to is connected with a set of electrical control cabinet containing the MVR evaporative crystallizer of organism Waste water concentrating crystallization, the Controlling System of described pneumatic adjusting valve and liquid level sensor and electrical control cabinet forms charging automatic control system, described feeding control system, the control end of automatic train control system is positioned at described housing, described housing is provided with the communication connection of Ethernet interface for same master control room.
The described saliferous that is applicable to is provided with a feed rate Controlling System containing the opening for feed of MVR evaporative crystallizer the 5th single-effect evaporator of organism Waste water concentrating crystallization, described feed rate Controlling System comprises a liquid level sensor and a pneumatic adjusting valve, the open degree of described pneumatic adjusting valve presses the level value auto-adjustment control of described liquid level sensor setting, the set(ting)value of described liquid level sensor presses the necessary level set of described 5th single-effect evaporator, the described saliferous that is applicable to is connected with a set of electrical control cabinet containing the MVR evaporative crystallizer of organism Waste water concentrating crystallization, the Controlling System of described pneumatic adjusting valve and liquid level sensor and electrical control cabinet forms charging automatic control system, described feeding control system, the control end of automatic train control system is positioned at described housing, described housing is provided with the communication connection of Ethernet interface for same master control room.
The described MVR evaporative crystallizer main body one being applicable to saliferous and containing the crystallization of organism Waste water concentrating, three, four, the well heater supplementary heating steam inlets of five effect bodies are provided with pneumatic adjusting valve and pressure unit or temperature transmitter, the open degree of described pneumatic adjusting valve presses the set(ting)value auto-adjustment control of described pressure unit or temperature transmitter, the set(ting)value of described pressure unit or temperature transmitter is by being applicable to the MVR evaporative crystallizer one of saliferous containing the crystallization of organism Waste water concentrating, three, four, the designed breeding setting of the well heater of five effect bodies and parameters revision setting when pressing equipment actual motion, the described saliferous that is applicable to is connected with a set of electrical control cabinet containing the MVR evaporative crystallizer of organism Waste water concentrating crystallization, the Controlling System of described pneumatic adjusting valve and pressure unit and temperature transmitter and electrical control cabinet forms heating automatic control system, described heating control system, the control end of automatic train control system is positioned at described housing, described housing is provided with the communication connection of Ethernet interface for same master control room.
Beneficial effect: owing to have employed technique scheme, the utility model adopt saliferous containing MVR (mechanically compress) double-effect evaporation of organism Waste water concentrating crystallization concentrated+single-effect evaporation is concentrated+dual evaporation crystallization technique, can effectively the suitability of MVR evaporating, concentrating and crystallizing be adopted to provide safeguard to saliferous containing the crystallization of organism Waste water concentrating, effectively can ensure recycling close to whole of water source, inorganic salt also can be recycled close to whole crystallization, it is little that treatment capacity arranged outward by high dense organic concentrated solution, can effectively realize heat energy close to 100% recycling utilization, ensure that the safety of saliferous containing the crystallization of organism Waste water concentrating, energy-conservation, the ideal performance of each side such as environmental protection.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Embodiment
The technique means realized to make the utility model, creation characteristic, reaching object and effect is easy to understand, setting forth the utility model further below in conjunction with concrete diagram.
With reference to schematic diagram 1, be applicable to the MVR evaporative crystallizer of saliferous containing the crystallization of organism Waste water concentrating, comprise five effect bodies, wherein the first effect body 1 is for the first time evaporation concentration of saliferous containing organic wastewater, comprise an effect well heater, imitate that well heater is connected with one one imitates evaporator room, second effect body 2 is for the second time evaporation concentration of saliferous containing organic wastewater, comprise to imitate with one that evaporator room is connected two imitate well heater, imitate that well heater is connected with two two imitate evaporator room, triple effect body 3 is for the third time evaporation concentration of saliferous containing organic wastewater, comprise the well heater of triple effect body 3, the evaporator room of the triple effect body 3 be connected with triple effect body 3 well heater, quadruple effect body 4 is for four evaporation concentration and the crystallization of saliferous containing organic wastewater, comprise the well heater of quadruple effect body 4, the evaporator room of the quadruple effect body 4 be connected with quadruple effect body 4 well heater, 5th effect body 5 is for five evaporation concentration and the crystallization of saliferous containing organic wastewater, comprise the well heater of the 5th effect, the 5th evaporator room of imitating be connected with the 5th effect well heater, comprise and second, three, four, the mechanical compressor that the evaporator room of five effects or crystallisation chamber are connected, the outlet of mechanical compressor is again with first, three, four, the heat ingress of the well heater of five effects is connected.The secondary steam that first effect body 1 evaporates enters the second effect body 2 well heater as heat source, is discharged after the water of condensation after heat source completes heat exchange is collected into condensation water collection tank by pump 6; Second and third, four, five effect evaporation secondary steams heat rear feeding first and third, four, five effect well heaters as heat source by mechanical compressor supercharging, discharged by pump 6 after the water of condensation after heat source completes heat exchange is collected into condensation water collection tank.
Be applicable to saliferous containing the MVR evaporative crystallizer of organism Waste water concentrating crystallization second and third, the outlets of secondary steam of four, five effect evaporations are provided with a mechanical compressor 7, can return after heating for evaporated secondary steam supercharging first and third, four, five effect as heating steam, achieve heat energy close to 100% recycling utilization.
Be applicable to the opening for feed that saliferous imitates body 1 vaporizer containing the MVR evaporative crystallizer first of organism Waste water concentrating crystallization and be provided with a feed rate Controlling System, feed rate Controlling System comprises a liquid level sensor and a pneumatic adjusting valve, the open degree of pneumatic adjusting valve presses the level value auto-adjustment control of liquid level sensor setting, the set(ting)value of liquid level sensor imitates the necessary level set of body 1 vaporizer by first, be applicable to saliferous and be connected with a set of electrical control cabinet containing the MVR evaporative crystallizer of organism Waste water concentrating crystallization, the Controlling System of pneumatic adjusting valve and liquid level sensor and electrical control cabinet forms charging automatic control system, feeding control system, the control end of automatic train control system is positioned at housing, housing is provided with the communication connection of Ethernet interface for same master control room.
Be applicable to the opening for feed that saliferous imitates body 2 vaporizer containing the MVR evaporative crystallizer second of organism Waste water concentrating crystallization and be provided with a feed rate Controlling System, feed rate Controlling System comprises a liquid level sensor and a pneumatic adjusting valve, the open degree of pneumatic adjusting valve presses the level value auto-adjustment control of liquid level sensor setting, the set(ting)value of liquid level sensor imitates the necessary level set of body 2 vaporizer by second, be applicable to saliferous and be connected with a set of electrical control cabinet containing the MVR evaporative crystallizer of organism Waste water concentrating crystallization, the Controlling System of pneumatic adjusting valve and liquid level sensor and electrical control cabinet forms charging automatic control system, feeding control system, the control end of automatic train control system is positioned at housing, housing is provided with the communication connection of Ethernet interface for same master control room.
Be applicable to saliferous and be provided with a feed rate Controlling System containing the opening for feed of MVR evaporative crystallizer triple effect body 3 vaporizer of organism Waste water concentrating crystallization, feed rate Controlling System comprises a liquid level sensor and a pneumatic adjusting valve, the open degree of pneumatic adjusting valve presses the level value auto-adjustment control of liquid level sensor setting, the set(ting)value of liquid level sensor presses the necessary level set of triple effect body 3 vaporizer, be applicable to saliferous and be connected with a set of electrical control cabinet containing the MVR evaporative crystallizer of organism Waste water concentrating crystallization, the Controlling System of pneumatic adjusting valve and liquid level sensor and electrical control cabinet forms charging automatic control system, feeding control system, the control end of automatic train control system is positioned at housing, housing is provided with the communication connection of Ethernet interface for same master control room.
Be applicable to saliferous and be provided with a feed rate Controlling System containing the opening for feed of MVR evaporative crystallizer quadruple effect body 4 vaporizer of organism Waste water concentrating crystallization, feed rate Controlling System comprises a liquid level sensor and a pneumatic adjusting valve, the open degree of pneumatic adjusting valve presses the level value auto-adjustment control of liquid level sensor setting, the set(ting)value of liquid level sensor presses the necessary level set of quadruple effect body 4 vaporizer, be applicable to saliferous and be connected with a set of electrical control cabinet containing the MVR evaporative crystallizer of organism Waste water concentrating crystallization, the Controlling System of pneumatic adjusting valve and liquid level sensor and electrical control cabinet forms charging automatic control system, feeding control system, the control end of automatic train control system is positioned at housing, housing is provided with the communication connection of Ethernet interface for same master control room.
Be applicable to saliferous and be provided with a feed rate Controlling System containing the opening for feed of MVR evaporative crystallizer the 5th single-effect evaporator of organism Waste water concentrating crystallization, feed rate Controlling System comprises a liquid level sensor and a pneumatic adjusting valve, the open degree of pneumatic adjusting valve presses the level value auto-adjustment control of liquid level sensor setting, the set(ting)value of liquid level sensor presses the necessary level set of the 5th single-effect evaporator, be applicable to saliferous and be connected with a set of electrical control cabinet containing the MVR evaporative crystallizer of organism Waste water concentrating crystallization, the Controlling System of pneumatic adjusting valve and liquid level sensor and electrical control cabinet forms charging automatic control system, feeding control system, the control end of automatic train control system is positioned at housing, housing is provided with the communication connection of Ethernet interface for same master control room.
Be applicable to the MVR evaporative crystallizer main body one of saliferous containing the crystallization of organism Waste water concentrating, three, four, five effect well heater supplementary heating steam inlets are provided with pneumatic adjusting valve and pressure unit or temperature transmitter, the open degree pressing force transmitter of pneumatic adjusting valve or the set(ting)value auto-adjustment control of temperature transmitter, the set(ting)value of pressure unit or temperature transmitter is by being applicable to the MVR evaporative crystallizer one of saliferous containing the crystallization of organism Waste water concentrating, three, four, the designed breeding setting of five effect well heaters and parameters revision setting when pressing equipment actual motion, be applicable to saliferous and be connected with a set of electrical control cabinet containing the MVR evaporative crystallizer of organism Waste water concentrating crystallization, the Controlling System of pneumatic adjusting valve and pressure unit and temperature transmitter and electrical control cabinet forms heating automatic control system, heating control system, the control end of automatic train control system is positioned at housing, housing is provided with the communication connection of Ethernet interface for same master control room, to realize intelligent management object.
Be provided with a filtration module in water of condensation water channel between condensate water pot and pump 6, filtration module, from the front carbon filter core being then followed successively by bright and beautiful logical sequence filter screen, regulating pH value resin, sinter containing 5 μm, regulates outside pH value resin and is surrounded by PP cotton.With the impurity in filter freezing water, the pH value regulating water of condensation, thus in wastewater treatment process, avoid the secondary pollution of water.
The foregoing describe ultimate principle of the present utility model and principal character and advantage of the present utility model.The technician of the industry should understand; the utility model is not restricted to the described embodiments; what describe in above-described embodiment and specification sheets just illustrates principle of the present utility model; under the prerequisite not departing from the utility model spirit and scope; the utility model also has various changes and modifications, and these changes and improvements all fall within the scope of claimed the utility model.The claimed scope of the utility model is defined by appending claims and equivalent thereof.
Claims (5)
1. be applicable to the MVR evaporative crystallizer of saliferous containing the crystallization of organism Waste water concentrating, comprise effect body, described effect body comprises vaporizer body, and described vaporizer body comprises well heater, the separate chamber be connected with described well heater or crystallisation chamber;
It is characterized in that, effect body has five, is the first effect body, the second effect body, triple effect body, quadruple effect body, the 5th effect body respectively; Described first effect body, the second effect body composition double-effect evaporator, described triple effect body is single-effect evaporator, and described quadruple effect body is single-effect evaporation crystallizer, and described 5th effect body is single-effect evaporation crystallizer;
Separate chamber's outlet of described first effect body is connected with the described second heat ingress of imitating the well heater of body, described second and third, four, five effect the separate chambers of body or the outlet of crystallisation chamber be connected with a mechanical compressor import, described mechanical compressor outlet is connected with described first and third, four, five heat ingress of imitating the well heater of body
2. the MVR evaporative crystallizer being applicable to saliferous and containing the crystallization of organism Waste water concentrating according to claim 1, it is characterized in that: the secondary steam of described first effect evacuator body enters the well heater of the second effect body as heat source, and the water of condensation after described heat source completes heat exchange is collected to condensate water pot;
Described second and third, four, five effect evacuator bodies water vapors by mechanical compressor supercharging heat rear feeding first and third, four, five effect body well heater as heat source, discharged by pump after the water of condensation after described heat source completes heat exchange is collected to condensate water pot.
3. the MVR evaporative crystallizer being applicable to saliferous and containing the crystallization of organism Waste water concentrating according to claim 2, it is characterized in that: in the feed system of five effect bodies, be equipped with liquid level sensor, the first pneumatic adjusting valve, the nourishing to fill in steam system and be equipped with pressure unit or temperature transmitter, the second pneumatic adjusting valve of five effect bodies, described liquid level sensor, described pressure unit or temperature transmitter, described first pneumatic adjusting valve, described second pneumatic adjusting valve connect a Controlling System respectively.
4. the MVR evaporative crystallizer being applicable to saliferous and containing the crystallization of organism Waste water concentrating according to claim 3, it is characterized in that: the opening for feed place of five effect bodies is equipped with liquid level sensor and charging autocontrol valve, and described liquid level sensor, described charging autocontrol valve connect a Controlling System.
5. the MVR evaporative crystallizer being applicable to saliferous and containing the crystallization of organism Waste water concentrating according to claim 3, it is characterized in that: the nourishing of five effect bodies is filled steam port place and be provided with pressure unit or temperature transmitter and admission autocontrol valve, described pressure unit or temperature transmitter, described admission autocontrol valve connect a Controlling System.
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| CN201420872892.XU CN204454673U (en) | 2014-12-29 | 2014-12-29 | Be applicable to the MVR evaporative crystallizer of saliferous containing the crystallization of organism Waste water concentrating |
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| CN201420872892.XU CN204454673U (en) | 2014-12-29 | 2014-12-29 | Be applicable to the MVR evaporative crystallizer of saliferous containing the crystallization of organism Waste water concentrating |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106395947A (en) * | 2016-11-03 | 2017-02-15 | 南京格洛特环境工程股份有限公司 | Dual-medium evaporative crystallization device and process |
| CN106422399A (en) * | 2016-09-22 | 2017-02-22 | 深圳市捷晶能源科技有限公司 | Energy-efficient evaporative concentration and crystallization system for salt solution and control method of system |
| CN106986358A (en) * | 2017-04-13 | 2017-07-28 | 安徽广信农化股份有限公司 | A kind of purifying technique of pyraclostrobin by-product sodium sulphate |
| CN108217794A (en) * | 2018-03-22 | 2018-06-29 | 兰州节能环保工程有限责任公司 | It is a kind of can simultaneously a variety of waste liquids of crystallization treatment method and device |
| CN108404443A (en) * | 2017-02-09 | 2018-08-17 | 欧洲技术设于伊特根的三聚氰氨，卢森堡，分支机构 | Melamine crystallization apparatus and the equipment for using the device |
| CN113476874A (en) * | 2021-07-29 | 2021-10-08 | 上海神农节能环保科技股份有限公司 | Multiple-effect evaporation crystallizer suitable for viscose fiber acid bath concentration crystallization |
| CN113476873A (en) * | 2021-07-29 | 2021-10-08 | 上海神农节能环保科技股份有限公司 | Multi-effect evaporator suitable for viscose fiber spinning scouring water concentration |
| CN114230085A (en) * | 2021-12-20 | 2022-03-25 | 安徽金禾实业股份有限公司 | Method for deep treatment and desalination of sucralose wastewater |
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2014
- 2014-12-29 CN CN201420872892.XU patent/CN204454673U/en active Active
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106422399A (en) * | 2016-09-22 | 2017-02-22 | 深圳市捷晶能源科技有限公司 | Energy-efficient evaporative concentration and crystallization system for salt solution and control method of system |
| CN106395947A (en) * | 2016-11-03 | 2017-02-15 | 南京格洛特环境工程股份有限公司 | Dual-medium evaporative crystallization device and process |
| CN108404443A (en) * | 2017-02-09 | 2018-08-17 | 欧洲技术设于伊特根的三聚氰氨，卢森堡，分支机构 | Melamine crystallization apparatus and the equipment for using the device |
| CN106986358A (en) * | 2017-04-13 | 2017-07-28 | 安徽广信农化股份有限公司 | A kind of purifying technique of pyraclostrobin by-product sodium sulphate |
| CN108217794A (en) * | 2018-03-22 | 2018-06-29 | 兰州节能环保工程有限责任公司 | It is a kind of can simultaneously a variety of waste liquids of crystallization treatment method and device |
| CN113476874A (en) * | 2021-07-29 | 2021-10-08 | 上海神农节能环保科技股份有限公司 | Multiple-effect evaporation crystallizer suitable for viscose fiber acid bath concentration crystallization |
| CN113476873A (en) * | 2021-07-29 | 2021-10-08 | 上海神农节能环保科技股份有限公司 | Multi-effect evaporator suitable for viscose fiber spinning scouring water concentration |
| CN114230085A (en) * | 2021-12-20 | 2022-03-25 | 安徽金禾实业股份有限公司 | Method for deep treatment and desalination of sucralose wastewater |
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| CP03 | Change of name, title or address |
Address after: 201300 Shanghai city Pudong New Area Town Road No. 211 Xuan Xuan Patentee after: SHANGHAI SENON CO., LTD. Address before: 201300 Shanghai city Pudong New Area Xuanqiao town Sanzao Industrial Zone, Road No. 211. Patentee before: Shanghai Senon Machinery Co., Ltd. |