CN105664511A - Continuous evaporation crystallization drying all-in-one machine - Google Patents
Continuous evaporation crystallization drying all-in-one machine Download PDFInfo
- Publication number
- CN105664511A CN105664511A CN201610115215.7A CN201610115215A CN105664511A CN 105664511 A CN105664511 A CN 105664511A CN 201610115215 A CN201610115215 A CN 201610115215A CN 105664511 A CN105664511 A CN 105664511A
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- Prior art keywords
- heating
- hot plate
- heating plate
- heat
- integrated machine
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/0082—Regulation; Control
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/0011—Heating features
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/0011—Heating features
- B01D1/0017—Use of electrical or wave energy
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/0011—Heating features
- B01D1/0041—Use of fluids
- B01D1/0047—Use of fluids in a closed circuit
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/0063—Control or regulation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D2009/0086—Processes or apparatus therefor
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Crystallography & Structural Chemistry (AREA)
- Drying Of Solid Materials (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention discloses a continuous evaporation crystallization drying all-in-one machine, comprising a PLC (programmable logic controller) control system, and a heating system and a rotating system which are connected with the PLC control system, wherein a main shaft of the rotating system is provided with a heating plate, a middle position of the heating plate is connected with the heating system, the upper end of the heating plate is provided with a nozzle connected to an original water tank by using a water inlet pipeline, the upper end of the heating plate is further provided with a steam recycling pipeline connected to a condenser, the condenser is connected with a distilled water collecting box, an original water return pipeline is arranged under the heating plate, and is connected to the original water tank, the lower end of the heating plate is further provided with a scraper near to the heating plate, the scraped dry powder is conveyed to the collecting box through a transport system, the heating plate can heat substance through various methods, such as rotating electrical heating, thermal cycling heating system heating, and the like, air energy heating can also be matched, and a heat-conducting and conductive slip ring fixed block is arranged at the rear end. According to the continuous evaporation crystallization drying all-in-one machine, the energy recycling is realized, the energy utilization rate is high, the temperature can be freely adjusted according to the PLC controller adopted by a user, a heating method is rotating heating, and the continuous evaporation crystallization drying all-in-one machine has the advantages of environmental protection, uniform heating, thorough evaporation, reuse of heat, and reuse of steam by equipping a condensing unit.
Description
Technical field
Present invention relates particularly to a kind of continuous evaporative crystallization dry integrated machine.
Background technology
The shortcomings such as dehydrator has a variety of, and the dehydrator of liquid wherein has RD multi-layer multi-stage multiple-effect liquid dried device, GLP centrifugal spray dryer etc., and it is too low that the former exists energy utilization rate, and structure is excessively complicated; The latter exists again that energy consumption is significantly high, and treating capacity is little, and floor space is big, and processing cost is high, and the problem such as exhaust emissions amount is excessive.
Summary of the invention
The present invention provides a kind of energy utilization rate continuous evaporative crystallization dry integrated machine thoroughly high, dry.
In order to solve above technical problem, the present invention adopts the technical scheme that:
Continuous evaporative crystallization dry integrated machine includes PLC control system and the heating system being connected with PLC control system and rotary system, the main shaft of described rotary system is provided with heating flow channel and heating system, described heating system includes adding hot plate, the described hot plate upper end that adds is provided with the shower nozzle being connected to raw water box with inlet channel, the described hot plate upper end that adds is additionally provided with and is connected to pressure charging system and is circulated heating, the remaining steam Steam Recovery pipeline by condenser, described condenser connects again distilled water collecting box, described heating is tried to get to the heart of a matter and is arranged with former water water return pipeline, described former water water return pipeline is connected to raw water box, the described hot plate lower end that adds is additionally provided with to press close to add the scraper of hot plate, described scraper one end is fixedly installed collecting box, dry powder is by induction system to collecting box, the moisture control of dry powder is below 10%, the described hot plate that adds can by multiple method, material heats, such as electric rotating heating, thermal cycle heating system heats etc., can also can heat by supporting air, and rear end is provided with heat conduction, conducting slip ring fixed block.
Preferably, described heating system mainly has heat-conducting oil heating, electrical heating, air to heat and the various ways such as steam heating.
Preferably, the mixing liquid of the various waste liquids such as described raw water box is dry containing solid-liquid built with needing, liquid high in salt, high solubility liquid, ionic liquid.
Preferably, described heating system and heat conduction article are constantly in continuous rotation status with main shaft.
Preferably, add hot plate described in be fabricated to by various Heat Conduction Materials and composite material.
Preferably, the rotary speed of heating-up temperature and rotary system that described PLC controls heating system controls the aridity of powder body and the moisture content of powder.
After adopting technique scheme, heat energy recycles, the heat produced by equipment realizes thermal cycle utilization by configuring equipment and system, by condensing unit by distilled water reuse, the moisture content of dry powder can control can also carry out moisture content adjustment according to the requirement of client below 10%, energy utilization rate is high, temperature adopts PLC freely to adjust according to client, mode of heating is rotary heating, there is environmental protection, homogeneous heating, thoroughly, steam is equipped with condensing unit and carries out the advantages such as reuse in evaporation.
Accompanying drawing explanation
In order to be illustrated more clearly that the embodiment of the present invention or technical scheme of the prior art, the accompanying drawing used required in embodiment or description of the prior art will be briefly described below, apparently, accompanying drawing in the following describes is some embodiments of the present invention, for those of ordinary skill in the art, under the premise not paying creative work, it is also possible to obtain other accompanying drawing according to these accompanying drawings.
Fig. 1 be continuous evaporative crystallization dry integrated machine of the present invention adopt conduction material be mode of heating realize block diagram;
Fig. 2 is the topology view that employing heating system is mode of heating one of continuous evaporative crystallization dry integrated machine of the present invention;
Fig. 3 is the topology view that employing heating system is mode of heating two of continuous evaporative crystallization dry integrated machine of the present invention;
Fig. 4 is the heat conduction of continuous evaporative crystallization dry integrated machine of the present invention, conducting slip ring fixed block;
Fig. 5 be continuous evaporative crystallization dry integrated machine of the present invention add hot plate sectional view.
1-main shaft 2-adds the hot plate 3-heating system 4-scraper 5-collecting box 6-heat conduction slip ring fixed block former water water return pipeline of 8-heating flow channel 9-.
Detailed description of the invention
For making the purpose of the embodiment of the present invention, technical scheme and advantage clearly, below in conjunction with the accompanying drawing in the embodiment of the present invention, technical scheme in the embodiment of the present invention is clearly and completely described, obviously, described embodiment is a part of embodiment of the present invention, rather than whole embodiments. Based on the embodiment in the present invention, all other embodiments that those of ordinary skill in the art obtain under not making creative work premise, broadly fall into the scope of protection of the invention.
Continuous evaporative crystallization dry integrated machine shown in accompanying drawings, including PLC control system and the heating system 3 being connected with PLC control system and rotary system, the main shaft 1 of described rotary system is provided with heating flow channel 8 and heating system 3, described heating system 3 includes adding hot plate 2, described hot plate 2 upper end that adds is provided with the shower nozzle being connected to raw water box with inlet channel, described hot plate 2 upper end that adds is additionally provided with and is connected to pressure charging system and is circulated heating, the remaining steam Steam Recovery pipeline by condenser, described condenser connects again distilled water collecting box, described heating is tried to get to the heart of a matter and is arranged with former water water return pipeline 9, described former water water return pipeline 9 is connected to raw water box, the described hot plate lower end that adds is additionally provided with the scraper 4 pressing close to add hot plate, described scraper 4 one end is fixedly installed collecting box 5, dry powder is by induction system to collecting box, the moisture control of powder is below 10%, the described hot plate 2 that adds can by multiple method, material heats, such as electric rotating heating, thermal cycle heating system heats etc., can also can heat by supporting air, and rear end is provided with heat conduction, conducting slip ring fixed block 6.
Described heating system 3 mainly has heat-conducting oil heating, electrical heating, air to heat and the various ways such as steam heating.
The mixing liquid of the various waste liquids such as described raw water box is dry containing solid-liquid built with needing, liquid high in salt, high solubility liquid, ionic liquid.
Described heating system and heat conduction article are constantly in continuous rotation status with main shaft.
The described hot plate that adds is fabricated to by various Heat Conduction Materials and composite material.
The rotary speed of heating-up temperature and rotary system that described PLC controls heating system controls the aridity of powder body and the moisture content of powder.
After adopting technique scheme, heat energy recycles, the heat produced by equipment realizes thermal cycle utilization by configuring equipment and system, by condensing unit by distilled water reuse, the moisture content of dry powder can control can also carry out moisture content adjustment according to the requirement of client below 10%, energy utilization rate is high, temperature adopts PLC freely to adjust according to client, mode of heating is rotary heating, there is environmental protection, homogeneous heating, thoroughly, steam is equipped with condensing unit and carries out the advantages such as reuse in evaporation.
Last it is noted that above example only illustrates technical scheme, it is not intended to limit; Although the present invention being described in detail with reference to previous embodiment, it will be understood by those within the art that: the technical scheme described in foregoing embodiments still can be modified by it, or wherein portion of techniques feature is carried out equivalent replacement; And these amendments or replacement, do not make the essence of appropriate technical solution depart from the spirit and scope of various embodiments of the present invention technical scheme.
Claims (6)
1. continuous evaporative crystallization dry integrated machine, it is characterized in that: include PLC control system and the heating system being connected with PLC control system and rotary system, the main shaft of described rotary system is provided with heating flow channel and heating system, described heating system includes adding hot plate, the described hot plate upper end that adds is provided with the shower nozzle being connected to raw water box with inlet channel, the described hot plate upper end that adds is additionally provided with and is connected to pressure charging system and is circulated heating, the remaining steam Steam Recovery pipeline by condenser, described condenser connects again distilled water collecting box, described heating is tried to get to the heart of a matter and is arranged with former water water return pipeline, described former water water return pipeline is connected to raw water box, the described hot plate lower end that adds is additionally provided with to press close to add the scraper of hot plate, described scraper one end is fixedly installed collecting box, dry powder delivers to collecting box by induction system, the moisture control of dry powder is below 10%, the described hot plate that adds can by multiple method, material heats, such as electric rotating heating, thermal cycle heating system heats, can also can heat by supporting air, and rear end is provided with heat conduction, conducting slip ring fixed block.
2. continuous evaporative crystallization dry integrated machine according to claim 1, it is characterised in that: described heating system mainly has heat-conducting oil heating, electrical heating, air can heat and steam heating.
3. continuous evaporative crystallization dry integrated machine according to claim 1, it is characterised in that: the mixing liquid of the various waste liquids such as described raw water box is dry containing solid-liquid built with needing, liquid high in salt, high solubility liquid, ionic liquid.
4. continuous evaporative crystallization dry integrated machine according to claim 1, it is characterised in that: described heating system and heat conduction article are constantly in continuous rotation status with main shaft.
5. continuous evaporative crystallization dry integrated machine according to claim 1, it is characterised in that: the rotary speed of temperature and electric rotating machine that described PLC controls heating system controls the aridity of powder body and the moisture content of powder.
6. continuous evaporative crystallization dry integrated machine according to claim 1, it is characterised in that: described in add hot plate and be fabricated to by various Heat Conduction Materials and composite material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610115215.7A CN105664511A (en) | 2016-03-01 | 2016-03-01 | Continuous evaporation crystallization drying all-in-one machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610115215.7A CN105664511A (en) | 2016-03-01 | 2016-03-01 | Continuous evaporation crystallization drying all-in-one machine |
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| Publication Number | Publication Date |
|---|---|
| CN105664511A true CN105664511A (en) | 2016-06-15 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
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| CN201610115215.7A Pending CN105664511A (en) | 2016-03-01 | 2016-03-01 | Continuous evaporation crystallization drying all-in-one machine |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106115822A (en) * | 2016-08-09 | 2016-11-16 | 江苏金陵干燥科技有限公司 | High-salt wastewater vacuum continuous evaporation dry integrated machine |
| CN108619745A (en) * | 2017-03-24 | 2018-10-09 | 天津邦特磁性材料有限公司 | A kind of full-automatic concentration systems of neodymium iron boron waste material filtrate |
| CN110947191A (en) * | 2018-09-27 | 2020-04-03 | 韩林辰 | Contact evaporation system |
| CN112079512A (en) * | 2020-09-24 | 2020-12-15 | 南宁腾宁商品混凝土有限公司 | Concrete production wastewater recovery device |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3043166A1 (en) * | 1980-11-15 | 1982-09-09 | Adalbert Klein, Apparatebau, 5905 Freudenberg | Vacuum slurry dryer with rotary plates and scrapers - is connected to condenser through filter wall retaining dust |
| CN2054159U (en) * | 1989-01-19 | 1990-03-07 | 卞作民 | Rotary disc type heating dryer |
| CN2139846Y (en) * | 1992-12-01 | 1993-08-11 | 沈善明 | Turntable evaporate concentrate machine |
| CN2196769Y (en) * | 1994-03-17 | 1995-05-10 | 李树海 | High-efficiency energy-saving disk type dryer |
| WO2015189864A1 (en) * | 2014-06-12 | 2015-12-17 | Hedinn Hf. | Apparatus for cooking and drying organic material |
| CN205494996U (en) * | 2016-03-01 | 2016-08-24 | 浙江菲尔特过滤科技有限公司 | Evaporate dry all -in -one of crystallization in succession |
-
2016
- 2016-03-01 CN CN201610115215.7A patent/CN105664511A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3043166A1 (en) * | 1980-11-15 | 1982-09-09 | Adalbert Klein, Apparatebau, 5905 Freudenberg | Vacuum slurry dryer with rotary plates and scrapers - is connected to condenser through filter wall retaining dust |
| CN2054159U (en) * | 1989-01-19 | 1990-03-07 | 卞作民 | Rotary disc type heating dryer |
| CN2139846Y (en) * | 1992-12-01 | 1993-08-11 | 沈善明 | Turntable evaporate concentrate machine |
| CN2196769Y (en) * | 1994-03-17 | 1995-05-10 | 李树海 | High-efficiency energy-saving disk type dryer |
| WO2015189864A1 (en) * | 2014-06-12 | 2015-12-17 | Hedinn Hf. | Apparatus for cooking and drying organic material |
| CN205494996U (en) * | 2016-03-01 | 2016-08-24 | 浙江菲尔特过滤科技有限公司 | Evaporate dry all -in -one of crystallization in succession |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106115822A (en) * | 2016-08-09 | 2016-11-16 | 江苏金陵干燥科技有限公司 | High-salt wastewater vacuum continuous evaporation dry integrated machine |
| CN108619745A (en) * | 2017-03-24 | 2018-10-09 | 天津邦特磁性材料有限公司 | A kind of full-automatic concentration systems of neodymium iron boron waste material filtrate |
| CN110947191A (en) * | 2018-09-27 | 2020-04-03 | 韩林辰 | Contact evaporation system |
| CN112079512A (en) * | 2020-09-24 | 2020-12-15 | 南宁腾宁商品混凝土有限公司 | Concrete production wastewater recovery device |
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Application publication date: 20160615 |