CN110482633A - A kind of sewage treatment vaporising device - Google Patents
A kind of sewage treatment vaporising device Download PDFInfo
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- CN110482633A CN110482633A CN201910772210.5A CN201910772210A CN110482633A CN 110482633 A CN110482633 A CN 110482633A CN 201910772210 A CN201910772210 A CN 201910772210A CN 110482633 A CN110482633 A CN 110482633A
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- 239000010865 sewage Substances 0.000 title claims abstract description 58
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 63
- 230000005684 electric field Effects 0.000 claims abstract description 47
- 238000001704 evaporation Methods 0.000 claims abstract description 31
- 230000008020 evaporation Effects 0.000 claims abstract description 31
- 238000011084 recovery Methods 0.000 claims abstract description 28
- 238000009833 condensation Methods 0.000 claims abstract description 27
- 230000005494 condensation Effects 0.000 claims abstract description 27
- 238000004140 cleaning Methods 0.000 claims abstract description 18
- 239000002910 solid waste Substances 0.000 claims abstract description 15
- 238000004134 energy conservation Methods 0.000 claims abstract description 12
- 239000002918 waste heat Substances 0.000 claims abstract description 10
- 239000002912 waste gas Substances 0.000 claims description 12
- 238000004064 recycling Methods 0.000 claims description 7
- 238000013461 design Methods 0.000 claims description 6
- 239000011358 absorbing material Substances 0.000 claims description 4
- 238000012544 monitoring process Methods 0.000 claims description 3
- 239000002699 waste material Substances 0.000 claims description 3
- 239000012528 membrane Substances 0.000 claims description 2
- 230000036413 temperature sense Effects 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 10
- 238000000034 method Methods 0.000 abstract description 5
- 230000007613 environmental effect Effects 0.000 abstract description 4
- 238000009434 installation Methods 0.000 abstract description 3
- 238000000926 separation method Methods 0.000 abstract description 2
- 238000012545 processing Methods 0.000 description 6
- 239000011552 falling film Substances 0.000 description 5
- 239000010408 film Substances 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 3
- 238000009835 boiling Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 239000010410 layer Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000010025 steaming Methods 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000013065 commercial product Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009713 electroplating Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 238000005213 imbibition Methods 0.000 description 1
- 230000005906 menstruation Effects 0.000 description 1
- 229920002338 polyhydroxyethylmethacrylate Polymers 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 230000003319 supportive effect Effects 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/32—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by electrical effects other than those provided for in group B01D61/00
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/048—Purification of waste water by evaporation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/08—Thin film evaporation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/16—Nature of the water, waste water, sewage or sludge to be treated from metallurgical processes, i.e. from the production, refining or treatment of metals, e.g. galvanic wastes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
- C02F2201/007—Modular design
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/10—Energy recovery
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Water Supply & Treatment (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Analytical Chemistry (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The present invention relates to a kind of sewage treatment vaporising devices.Its main structure includes that high voltage electric field evaporative cylinder, induced draught system, waste heat of condensation energy conservation recovery system and plasma cleaning systems are constituted.The present invention, which only relies on discharge system, can complete the separation of water process and solid waste to the effect of tank body evaporator.Have the advantages that structure is simple, easy for installation, evaporation efficiency is high, high treating effect, operating cost are low, applied widely, environmental protection and energy saving.
Description
Technical field
The present invention relates to water treatment facilities, specifically, being a kind of sewage treatment vaporising device, belong to energy conservation and environmental protection neck
Domain.
Background technique
It is always at present hot issue to sewage treatment.Especially industrial electroplating sewerage, water is big, concentration is high, heavy metal
Ion weight is more, thus processing difficulty is big.The technology mostly used greatly at present is the processing of precipitation and purification multi-stage combination, by sedimentation, only
Change, liquid stream, precipitating, filtering etc. reach final emission treatment or centralized collection is sent to specialized company on behalf of processing.But it is this
Sewage disposal device generally requires biggish occupied area or higher construction cost to build, and process flow is complicated, energy consumption
Larger, operating cost is high.Promoting in medium-sized and small enterprises has significant limitation.
Traditional evaporator is evaporated mostly by heating to evaporate by numerous falling film evaporation pipelines.Can generate with
Lower disadvantage: 1. heating is heated by heating tube, and energy conversion efficiency is low.2. tiny falling film evaporator inner wall is steamed because sewage is heated
It sends out and crystallizes into dirt, thus serious blocking evaporator.The secondary returning 3. heat that the water vapour evaporated is directly taken away is had no idea
It receives and utilizes, energy consumption is high.
Summary of the invention
The present invention provides a kind of new energy-efficient sewage treatment vaporising device, the dirt for above-mentioned problem place
Water process vaporising device can effectively improve energy conversion efficiency, and depending merely on high voltage electric field evaporative cylinder this unit can accomplish to handle
A variety of wastes and different heavy metals simultaneously complete the processing of sewage and the separation of waste, can be with round-the-clock automatic operating.Tool
Have that structure is simple, easy for installation, evaporation efficiency is high, high treating effect, operating cost are low, applied widely, environmental protection and energy saving excellent
Point.
The technical solution adopted by the invention is as follows:
A kind of sewage treatment vaporising device, it is high voltage electric field evaporative cylinder A including the connection of from bottom to top sectional, induced draught system B, cold
Solidifying afterheat energy-saving recovery system C and low temperature plasma waste gas cleaning device D；
The condensation and afterheat energy-saving recovery system C include that one end goes out with cold sewage water inlet pipe C1, the other end with hot sewage
The shell-and-tube heat exchanger C3 of water pipe C2, circulating sewage in the tube side of the shell-and-tube heat exchanger C3, the shell-and-tube heat exchanger
Shell side is communicated with induced draught system B；
The hot sewage outlet pipe C2 of the condensation and afterheat energy-saving recovery system C are conducted to high voltage electric field via intermediate diversion pipeline
Inside evaporative cylinder A, it is connected with the inlet pipeline A1 of high voltage electric field evaporative cylinder A；
The annular water distributor A2 that the high voltage electric field evaporative cylinder A includes cylinder, depends on cylinder inboard wall and designs, and described
The discharge electrode A3 that body centre is set up；The annular water distributor A2 circumferentially offers watering of the circle opening towards cylinder inner wall
Hole flows down the sewage entered in high voltage electric field evaporative cylinder A along cylinder inboard wall by the water sprayering hole of annular water distributor and forms one
Layer moisture film；
The induced draught system B is located between high voltage electric field evaporative cylinder A and condensation and afterheat energy-saving recovery system C, using
Centrifugal blower B1 makes the high negative pressure environment that class vacuum is formed in evaporative cylinder, to evaporative cylinder exhausting to reduce the steam of evaporation interface
Pressure, further increases evaporation efficiency.
The sewage treatment vaporising device further includes control system E, the control system E include with control panel E5,
The cabinet case E1 of display screen and electrically operated valve, and the use being installed between induced draught system B and condensation and afterheat energy-saving recovery system C
In acquisition vapor (steam) temperature steam temperature sensor E2 and steam flow sensor E3 for acquiring steam flow, be installed on it is cold
It is solidifying between afterheat energy-saving recovery system and low temperature plasma waste gas cleaning device for acquire condense after temperature condenser temperature
Spend inductor E4；The steam temperature sensor E2, steam flow sensor E3 and condenser temperature inductor E4 are by acquisition
Related data is sent to control system E, from the real function of playing real-time monitoring and regulation；
The discharge electrode A3 is connected by power supply line A4 with control system E, provides electric energy to it by control system E, institute
The voltage design for stating discharge electrode A3 is 100KV, electric current 25-35mA；
The cold sewage water inlet pipe C1 is connected by water pump C4 with cesspool, before being equipped on the cold sewage water inlet pipe C1
Processing filters C5, the pretreatment filter C5 is using strainer.
Metering pump A8 is installed on the inlet pipeline A1 of the high voltage electric field evaporative cylinder A, is controlled and is entered by metering pump A8
Water inside evaporative cylinder.
In order to reach better evaporation effect, the inner wall of the evaporative cylinder adds water-absorbing material A5, such as felt；
The high voltage electric field evaporative cylinder A, induced draught system B, waste heat of condensation energy conservation recovery system C and low temperature plasma waste gas cleaning system
Unite D, they pass through flanged joint between each other；
The low temperature plasma waste gas cleaning device D is using existing commercial product.
The cylinder body bottom of the high voltage electric field evaporative cylinder A offers solid waste discharge outlet, in the solid waste discharge outlet
Lower part is equipped with solid waste recycling bins A9, and the solid waste of cylinder body bottom will can be periodically deposited on by the solid waste recycling bins A9
Object is emitted into outside cylinder.
A kind of sewage treatment vaporising device of the invention, structure is simple and direct, easy for installation, evaporation efficiency is high, high treating effect,
Operating cost is low, applied widely, energy conservation and environmental protection.By high voltage electric field evaporative cylinder, induced draught system, waste heat of condensation energy conservation recovery system
In a system with plasma cleaning systems series connection, sewage initially enters in waste heat of condensation energy conservation recovery system, more than condensation
Sewage after exchanging heat in thermal center energy recovery system enters in high voltage electric field evaporative cylinder, is formed via annular water distributor in cylinder inboard wall
The discharge electrode of moisture film, high voltage electric field evaporative cylinder center generates high-frequency and high-voltage alternating electric field, and hydrone receives the energy of alternating electric field
Amount is converted to water vapour, greatly improves sewage evaporation process and evaporation efficiency, evaporates the high-temperature water vapor of generation via top
Induced draught system is sent into afterheat energy-saving recovery system and plasma cleaning systems, to afterheat energy-saving recovery system and plasma cleaning
Sewage in system exchanges heat.Water vapour partial condensation after heat exchange is discharged at water, partially through low temperature plasma waste gas cleaning
It is discharged into atmospheric environment after device processing.
Detailed description of the invention
A kind of Fig. 1: sewage treatment vaporising device structural schematic diagram of the present invention；
A, high voltage electric field evaporative cylinder in the figure, A1, inlet pipeline, A2, annular water distributor, A3, discharge electrode, A4, power supply line,
A5, water-absorbing material, A6, support frame, A7, electrode support, A8, metering pump, B, induced draught system, B1, centrifugal blower, B2, condensation
Water outlet, C, waste heat of condensation energy conservation recovery system, C1, cold sewage water inlet pipe, C2, hot sewage outlet pipe, C3, pipe shell type heat exchange
Device, C4, water pump, C5, pretreatment filter, D, low temperature plasma waste gas cleaning system, E, control system, E1, cabinet case, E2, steaming
Stripping temperature sensor, E3, steam flow sensor, E4, condenser temperature inductor.
Specific embodiment
Attached drawing is described in detail below the present invention below.
Embodiment one
A kind of sewage treatment vaporising device, mainly by high voltage electric field evaporative cylinder A, induced draught system B, waste heat of condensation energy conservation recycling system
System C and low temperature plasma waste gas cleaning device D and control system E several major collectively form；High voltage electric field evaporative cylinder A therein,
Induced draught system B, waste heat of condensation energy conservation recovery system C and low temperature plasma waste gas cleaning device D are connected in range selector, logical between each other
It crosses flanged joint and forms whole vertical tank structure.High voltage electric field evaporative cylinder A therein is located at bottommost, installs in its underpart
There is the support frame A6 for playing a supportive role to overall structure.Induced draught system is connected in turn upwards along high voltage electric field evaporative cylinder A
B, waste heat of condensation energy conservation recovery system C and low temperature plasma waste gas cleaning device D.The condensation and afterheat energy-saving recovery system C are adopted
It is shell-and-tube heat exchanger, one end has cold sewage water inlet pipe C1, and the other end has hot sewage outlet pipe C2, the cold dirt
Water water inlet pipe C1 is connected via water pump C4 with cesspool, is equipped with sewage filter net on the cold sewage water inlet pipe C1, cold
Sewage enters inside heat exchanger after filtering before menstruation, passes through hot sewage outlet pipe C2 and intermediate diversion pipe after heat exchanger internal heat
Road is connected inside high voltage electric field evaporative cylinder A, is connected with the inlet pipeline A1 of high voltage electric field evaporative cylinder A；The high voltage electric field steams
The inlet pipeline A1 of hair cylinder A is equipped with metering pump A8, and the sewage quantity of inner barrel is entered by metering pump A8 control；The high pressure
The annular water distributor A2 that electric field evaporative cylinder A includes cylinder, depends on cylinder inboard wall and designs, and set up in the body centre
Discharge electrode A3；The annular water distributor A2 circumferentially offers water sprayering hole of the circle opening towards cylinder inner wall, by annular cloth
The water sprayering hole of water pipe A2 makes the sewage entered in high voltage electric field evaporative cylinder A flow down along cylinder inboard wall and form water membrane；It is described
Discharge electrode A3 is installed on body centre by electrode support A7, and in order to reach better evaporation effect, the high voltage electric field steams
The inner wall of hair cylinder A is attached with one layer of felt, by the water imbibition of felt, so that the sewage that annular water distributor A2 is flowed down persistently is kept
It is adsorbed on cylinder inboard wall, the energy for making more hydrones receive alternating electric field is converted into water vapour.Described induced draught system B
Between high voltage electric field evaporative cylinder A and condensation and afterheat energy-saving recovery system C, evaporative cylinder is taken out using centrifugal blower B1
Wind makes the high negative pressure environment for forming class vacuum in evaporative cylinder, to reduce the vapour pressure of evaporation interface, further increase evaporation effect
Rate.Hydrone is converted water vapour by high-frequency and high-voltage alternating electric field in high voltage electric field evaporative cylinder A, is born by top induced draught system
Pressure effect, high-temperature water vapor go upward to condensation and the afterheat energy-saving recovery system C at top, the cold dirt in this heat exchanging device tube side
Water exchanges heat, and after a part of water vapour is condensed into water, is discharged via the condensate drain outlet B2 of induced draught system lower part, another portion
Water vapour is divided to continue to go upward to low temperature plasma waste gas cleaning device, after further being purified via low temperature plasma waste gas cleaning device,
It is expelled to atmospheric environment.The control system E includes cabinet the case E1, Yi Jian with control panel, display screen and electrically operated valve
Loaded on the steam temperature sensor for being used to acquire vapor (steam) temperature between induced draught system B and condensation and afterheat energy-saving recovery system C
E2 and steam flow sensor E3 for acquiring steam flow, be installed on condensation and afterheat energy-saving recovery system and low temperature etc. from
Between sub- catalytic converter for acquire condense after temperature condenser temperature inductor E4；The steam temperature sensor
The related data of acquisition is sent to control system E, Cong Shiqi by E2, steam flow sensor E3 and condenser temperature inductor E4
To real-time monitoring and the function of regulation；The discharge electrode A3 is connected by power supply line A4 with control system E, is by control
System E provides it electric energy, and the voltage design of the discharge electrode A3 is 100KV, electric current 25-35mA.The high voltage electric field steams
The cylinder body bottom of hair cylinder A offers solid waste discharge outlet, is equipped with solid waste recycling bins in the lower part of the solid waste discharge outlet
The solid waste for being deposited on cylinder body bottom can be periodically emitted into outside cylinder by A9 by the solid waste recycling bins A9.
A kind of sewage treatment vaporising device of the invention is handed over using shallow river effect by the high pressure of high voltage electric field evaporative cylinder A
Changed electric field electric discharge destroys the surface tension of sewage surface layer, and energy needed for hydrone evaporation greatly reduces, the steaming of hydrone
Hair speed greatly increases.In addition to this, the application also analyzes the influence to evaporation capacity is improved in terms of wind pressure:
1KG water at one atm (normal pressure) from 25 degree be heated to 100 degree (reach boiling point and completely vaporize) needed for energy are as follows:
2257.9+313.5=2571.4kJ；
1KG water is heated to the energy needed for (reach boiling point and completely vaporize) that boils from 25 degree under negative pressure condition are as follows: 2293.6+
255=2548.6kJ；
By contrast, the two difference 22.8kJ/kg, about 10% or so, are to have an impact to evaporation by comparing visible subnormal ambient above
's.
The energy datum comparison of same one ton of water of evaporation see the table below:
| Evaporation equipment | Power consumption KW |
| Common evaporator | 210 |
| Falling film evaporator | 70 |
| The sewage treatment vaporising device of this patent | 40-50 |
Energy-efficient sewage treatment vaporising device of the invention, evaporation efficiency reach as high as 50-60 times of common evaporator.50-
10 times or more of evaporation rate can be improved in 60 times of origin, 100KV high voltage electric field, and negative pressure exhausting environment doubles a left side
The case where right evaporation rate, internal barrel water film evaporation leans on evaporation from water surface than one barrel of water of common evaporator, increases 7-10 times
Evaporation surface.
Sewage-treatment plant of the present invention has the technical effect that
1. the high-frequency and high-voltage alternating electric field generated using electrode, is substantially increased evaporation rate, hydrone is made to receive alternating electric field
Energy be converted to vapor.
2. directlying adopt evaporation tank body as falling film evaporator, water is set uniformly to form moisture film in inner wall by bucket inner wall,
Common falling film evaporation pipe is solved the problems, such as because of inefficiency caused by fouling blockage.
3. air-introduced machine to the low pressure of class vacuum, subnormal ambient is formed in evaporator, reduces water from liquid to gaseous state interface
Vapour pressure effectively accelerates evaporation rate.
4. the heat in flashes vapor heats heat transfer through sewage of the heat exchanger tube to water inlet pipe in evaporation tub, effectively return
Energy is utilized in receipts, promotes energy-saving and emission-reduction.
Claims (9)
1. a kind of sewage treatment vaporising device, high voltage electric field evaporative cylinder (A), induced draught system including the connection of from bottom to top sectional
(B), waste heat of condensation energy conservation recovery system (C) and plasma cleaning systems (D)；
The condensation and afterheat energy-saving recovery system (C) include that one end is dirty with heat with cold sewage water inlet pipe (C1), the other end
The shell-and-tube heat exchanger (C3) of water outlet pipe (C2), circulating sewage in the tube side of the shell-and-tube heat exchanger (C3), the shell
The shell side of formula heat exchanger is communicated with induced draught system (B)；
The hot sewage outlet pipe (C2) of the condensation and afterheat energy-saving recovery system (C) are conducted to high pressure via intermediate diversion pipeline
Electric field evaporative cylinder (A) is internal, is connected with the inlet pipeline (A1) of high voltage electric field evaporative cylinder (A)；
The annular water distributor (A2) that the high voltage electric field evaporative cylinder includes cylinder, depends on cylinder inboard wall and designs, and in institute
State the discharge electrode (A3) of body centre erection；The annular water distributor (A2) circumferentially offers circle opening towards cylinder inner wall
Water sprayering hole, by the water sprayering hole of annular water distributor make the sewage entered in high voltage electric field evaporative cylinder (A) flow down along cylinder inboard wall and
Form water membrane；
The induced draught system (B) is located between high voltage electric field evaporative cylinder (A) and condensation and afterheat energy-saving recovery system (C), adopts
It is centrifugal blower (B1) to evaporative cylinder exhausting, makes the high negative pressure environment for forming class vacuum in evaporative cylinder, reduces evaporation circle
The vapour pressure in face, further increases evaporation efficiency.
2. a kind of sewage treatment vaporising device as described in claim 1, is characterized in that,
The sewage treatment vaporising device further includes control system (E), and the control system (E) includes with control panel, shows
The cabinet case (E1) of display screen and electrically operated valve, and be installed between induced draught system (B) and condensation and afterheat energy-saving recovery system (C)
The steam temperature sensor (E2) for acquiring vapor (steam) temperature and steam flow sensor (E3) for acquiring steam flow,
Be installed between condensation and afterheat energy-saving recovery system and low temperature plasma waste gas cleaning device for acquire condense after temperature
Condenser temperature inductor (E4)；The steam temperature sensor (E2), steam flow sensor (E3) and condenser temperature sense
Answer device (E4) that the related data of acquisition is sent to control system (E), from the real function of playing real-time monitoring and regulation.
3. a kind of sewage treatment vaporising device as claimed in claim 2, is characterized in that,
The discharge electrode (A3) is connected by power supply line (A4) with control system (E), is provided by control system (E) it
Electric energy, the voltage design of the discharge electrode (A3) are 100KV, electric current 25-35mA.
4. a kind of sewage treatment vaporising device as claimed in claim 2, is characterized in that,
The cold sewage water inlet pipe (C1) is connected by water pump (C4) with cesspool, is pacified on the cold sewage water inlet pipe (C1)
Equipped with pretreatment filter (C5), the pretreatment filter (C5) is using strainer.
5. a kind of sewage treatment vaporising device as described in claim 1, is characterized in that,
The cylinder inboard wall of the high voltage electric field evaporative cylinder (A) is covered with water-absorbing material.
6. a kind of sewage treatment vaporising device as claimed in claim 5, is characterized in that,
The water-absorbing material is felt.
7. a kind of sewage treatment vaporising device as described in claim 1, is characterized in that,
The high voltage electric field evaporative cylinder (A), induced draught system (B), waste heat of condensation energy conservation recovery system (C) and plasma cleaning systems
(D) pass through flanged joint between.
8. a kind of sewage treatment vaporising device as described in claim 1, is characterized in that,
The cylinder body bottom of the high voltage electric field evaporative cylinder (A) offers solid waste discharge outlet, under the solid waste discharge outlet
Portion is equipped with solid waste recycling bins (A4), will can periodically be deposited on consolidating for cylinder body bottom by the solid waste recycling bins (A4)
Outside waste discharge to cylinder.
9. a kind of sewage treatment vaporising device as described in claim 1, is characterized in that,
Metering pump is installed on the inlet pipeline (A1) of the high voltage electric field evaporative cylinder (A), is controlled by metering pump and enters evaporation
Water inside cylinder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910772210.5A CN110482633A (en) | 2019-08-21 | 2019-08-21 | A kind of sewage treatment vaporising device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910772210.5A CN110482633A (en) | 2019-08-21 | 2019-08-21 | A kind of sewage treatment vaporising device |
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| Publication Number | Publication Date |
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| CN110482633A true CN110482633A (en) | 2019-11-22 |
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| CN201910772210.5A Pending CN110482633A (en) | 2019-08-21 | 2019-08-21 | A kind of sewage treatment vaporising device |
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20050011743A1 (en) * | 2001-10-13 | 2005-01-20 | Hernandez Fernando Maria Hernandez | Installation used to obtain salt-free sea water at a low temperature with continuous operation and enthalpy recovery |
| CN103170156A (en) * | 2013-04-10 | 2013-06-26 | 北京纬纶华业环保科技股份有限公司 | Low-temperature energy-efficient evaporative crystallization device and technology |
| CN206278945U (en) * | 2016-10-03 | 2017-06-27 | 南华大学 | A kind of high-voltage electrostatic field formula gas-liquid contact is concentrated by evaporation high-salt wastewater device |
| CN210825509U (en) * | 2019-08-21 | 2020-06-23 | 宋怡佳 | Sewage treatment evaporation plant |
-
2019
- 2019-08-21 CN CN201910772210.5A patent/CN110482633A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20050011743A1 (en) * | 2001-10-13 | 2005-01-20 | Hernandez Fernando Maria Hernandez | Installation used to obtain salt-free sea water at a low temperature with continuous operation and enthalpy recovery |
| CN103170156A (en) * | 2013-04-10 | 2013-06-26 | 北京纬纶华业环保科技股份有限公司 | Low-temperature energy-efficient evaporative crystallization device and technology |
| CN206278945U (en) * | 2016-10-03 | 2017-06-27 | 南华大学 | A kind of high-voltage electrostatic field formula gas-liquid contact is concentrated by evaporation high-salt wastewater device |
| CN210825509U (en) * | 2019-08-21 | 2020-06-23 | 宋怡佳 | Sewage treatment evaporation plant |
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