CN202315515U - Flue gas wet flue gas desulfurization gypsum rotary table dehydrator - Google Patents
Flue gas wet flue gas desulfurization gypsum rotary table dehydrator Download PDFInfo
- Publication number
- CN202315515U CN202315515U CN2011204488533U CN201120448853U CN202315515U CN 202315515 U CN202315515 U CN 202315515U CN 2011204488533 U CN2011204488533 U CN 2011204488533U CN 201120448853 U CN201120448853 U CN 201120448853U CN 202315515 U CN202315515 U CN 202315515U
- Authority
- CN
- China
- Prior art keywords
- slurry tank
- filtering table
- desulfurization gypsum
- smoke
- rotating disk
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn - After Issue
Links
Images
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model relates to a flue gas wet flue gas desulfurization gypsum rotary table dehydrator, which comprises a host system and a vacuum system, wherein the host system comprises an airframe, a slurry tank, a rotating device, a driving device, a discharge device and filter trays, the two ends of the slurry tank are fixed on the airframe, the rotating device is of a cylindrical structure, the two ends of the rotating device are fixed on the two ends of the slurry tank, the rotating device is driven by the driving device to rotate in the slurry tank, the rotating device is provided with a plurality of filter trays, the filter trays are ring-shaped tray shapes, each filter tray is arranged around the outer peripheral surface of the rotating device, cavities are arranged in the inner portions of the filter trays, the surfaces of the filter trays are provided with micropores which are communicated with the cavities, the discharge device is fixed on the slurry tank, and contacts with the surfaces of the filter trays, and the vacuum system is communicated with the cavities of the inner portions of the filter trays. The flue gas wet flue gas desulfurization gypsum rotary table dehydrator is reliable in performance, small in occupied area, low in energy consumption, low in maintenance cost of a switch, and excellent in dehydration effect.
Description
Technical field
The utility model relates to a kind of smoke-gas wet desulfurization gypsum rotating disk dewaterer, belongs to smoke-gas wet desulfurization gypsum dehydration field.
Background technology
Usually, power-plant flue gas is because of sulfur-bearing (SO
2) before its discharging, must through desulfurizer it be removed earlier.Lime stone-gypsum wet flue gas desulfurizing (FGD) system is generally adopted in flue gas desulfurization.Domestic at present and even most of in the world lime stone-gypsum method technology desulfurization (SO that adopts
2) thermal power plant of system adopts vacuum belt dewaterer to come its tail product is carried out Separation of Solid and Liquid.This vacuum belt dewaterer has technology maturation in the sector, dependable performance, simple operation and other advantages.But on the other hand, this vacuum belt dewaterer exists floor space big, and investment is high, and energy consumption is high, the shortcoming that filter liquor concentration height and maintenance cost are higher.
The utility model content
The purpose of the utility model is to solve the shortcoming that the traditional vacuum belt dewaterer uses on FGD, a series of problem of particularly in the power plant desulfurization transformation, bringing inadequately owing to the factory site provides a kind of smoke-gas wet desulfurization gypsum rotating disk dewaterer; It is a filtering surface with the facade, and it is big to have solved traditional vacuum belt dewaterer floor space, the shortcoming that energy consumption is high; Be a kind of dependable performance, floor space is little, and energy consumption is low; The switch maintenance cost is low, the high-quality dewaterer that dehydrating effect is good.
The technical scheme that the utility model solves the problems of the technologies described above is following: a kind of smoke-gas wet desulfurization gypsum rotating disk dewaterer; Comprise host computer system and vacuum system, said host computer system comprises frame, slurry tank, tumbler, drive unit, device for discharging and filtering table, and the two ends of said slurry tank are fixed on the said frame; Said tumbler is a cylindrical structural; Its two ends are fixed on the two ends of said slurry tank, and said drive unit drives said tumbler and in said slurry tank, rotates, and said tumbler is provided with a plurality of said filtering tables; Said filtering table is a ring discoid; Each filtering table is all around on the outer circumference surface that is arranged on said tumbler, and said filtering table inside has cavity, on the surface of said filtering table, is provided with the micropore that is connected with said cavity; Said device for discharging is fixed on the said slurry tank, and contacts with the surface of said filtering table; Said vacuum system is connected with the inner cavity of said filtering table.
Further; Said vacuum system comprises steam-water separator, vavuum pump and is connected flexible pipe; Said connection flexible pipe is distributed on the outer peripheral face of said tumbler; And be connected with the internal cavities of said filtering table, said steam-water separator connects with the said flexible pipe that is connected, and said vavuum pump is connected with said steam-water separator.
Further, also comprise purging system; Said purging system comprises agitating device, ultrasonic cleaning equipment, back purge system and chemically-cleaning device; Said agitating device and said ultrasonic cleaning equipment all are arranged in the said slurry tank; Said chemically-cleaning device is connected with said back purge system, and said back purge system is connected with the inner cavity of said filtering table through pipeline.
Further, said agitating device is that device is mixed in mechanical stirring device or gas mixing.
Further, said agitating device comprises the swing arm linkage and stirs decelerator that said stirring decelerator drives said swing arm linkage and in said slurry tank, moves.
Further, also comprise the control system; Said control system is connected with said host computer system, is used to control the on off state of said host computer system; Said control system is connected with said vacuum system, in order to control the on off state of said vacuum system; Said control system is connected with said purging system, is used to control the on off state of said purging system.
Further, said filtering table adopts disc that capillary ceramic plate, volcanic rock process as its filter medium.
Further, the bottom of said slurry tank is provided with charging void channels and plasma discharge hole, on the sidewall of said slurry tank, is provided with spout hole.
The beneficial effect of the utility model is; The utility model smoke-gas wet desulfurization gypsum rotating disk dewaterer is the advanced technology and the equipment in FGD field, and the filtering table inside that it is selected for use has cavity, the surface is provided with micropore; For the filtering table internal cavities vacuum is provided through vacuum system; Realization is carried out Separation of Solid and Liquid with the slurries that FGD produced, and has solved defective and deficiency that traditional vacuum belt dewaterer equipment is used in this field, compares with traditional vacuum belt dewaterer to have the following advantages:
1. the utility model smoke-gas wet desulfurization gypsum rotating disk dewaterer is through being arranged on the ring-type filtering table on the outer peripheral face of tumbler; The filtering surface that makes filtering table form is a facade; Having changed tradition is the vacuum belt dewaterer structure of filtering surface with the horizontal plane, effectively reduces the floor space of equipment.
2. the utility model smoke-gas wet desulfurization gypsum rotating disk dewaterer adopts and to have the potsherd of micropore or filtering table that other filter mediums are processed carries out Separation of Solid and Liquid to slurries; Its filtrating is as clear as crystal; Basically there is not solid particle; Can reuse, and traditional device is to be filter medium with the filter cloth that its filtrating solid content is high.
3. to compare its vacuum leak littler for the utility model smoke-gas wet desulfurization gypsum rotating disk dewaterer and traditional vacuum belt dewaterer, and equipment energy consumption is lower, saves energy consumption about 70%.
4. the utility model smoke-gas wet desulfurization gypsum rotating disk dewaterer and traditional vacuum belt dewaterer are compared, and the technology water consumption is lower, practice thrift fresh water (FW) and advance 50%.
5. the utility model smoke-gas wet desulfurization gypsum rotating disk dewaterer and traditional vacuum belt dewaterer are compared, this compact equipment, rationally, and dependable performance, stable, the switch maintenance cost is lower.
6. the utility model smoke-gas wet desulfurization gypsum rotating disk dewaterer is specially adapted to power plant's coal content height, the occasion that the dehydration equipment factory site is not enough.
Description of drawings
Fig. 1 is the structural representation of the utility model smoke-gas wet desulfurization gypsum rotating disk dewaterer.
The specific embodiment
Below in conjunction with accompanying drawing the principle and the characteristic of the utility model are described, institute gives an actual example and only is used to explain the utility model, is not the scope that is used to limit the utility model.
As shown in Figure 1, a kind of smoke-gas wet desulfurization gypsum rotating disk dewaterer comprises host computer system, vacuum system, purging system and control system.Host computer system comprises frame 11, slurry tank 12, tumbler 13, drive unit, device for discharging 15 and filtering table 16; The two ends of slurry tank 12 are fixed on the frame 11; The bottom of slurry tank 12 is provided with charging void channels 121 and plasma discharge hole 122; On the sidewall of slurry tank 12, be provided with spout hole 123, on slurry tank 12, also be provided with rinse mouth 124.Tumbler 13 is a cylindrical structural, and at the two ends of slurry tank 12, drive unit comprises drive motors 141 and drives reduction box 142 through bearing fixing at its two ends; Drive motors 141 is connected with driving reduction box 142 through shaft coupling, drives reduction box 142 and is connected with tumbler 13 through shaft coupling, and drive motors 141 drives reduction box 142 rotations; Drive reduction box 142 drive tumblers 13 and in slurry tank 12, rotate, tumbler 13 is provided with a plurality of filtering tables 16, and these a plurality of filtering tables 16 all adopt capillary ceramic plate to process; Each filtering table 16 is the annular disk structure; This annular disk is around on the outer circumference surface that is arranged on tumbler 13, and filtering table 16 inside have cavity, on the surface of filtering table 16, is provided with the micropore that is connected with its internal cavities; Device for discharging 15 is fixed on the slurry tank 12; These device for discharging 15 positions are corresponding with each filtering table 16 position, and device for discharging 15 contacts with the surface of filtering table 16, are used to lay down the filter cake of absorption on the filtering table 16.Host computer system is when switch; Slurries evenly get into slurry tank 12 bottoms by feed pipe 121; Avoid uneven load that filtering table 16 is impacted; Drive reduction box 142 and power is provided, and experience pulp absorbing area, filtering area, drip washing district, dry section, discharge zone and backwash district successively through tumbler 13 drive filtering tables 16 and accomplish whole filter process with drive motors 141.When slurries reached the appointment liquid level, unnecessary slurries will flow out from spout hole 123.When host computer system was shut down, remaining slurries were through 122 emptyings of plasma discharge hole in the slurry tank 12.
Vacuum system comprises steam-water separator 21, vavuum pump 22 and is connected flexible pipe 23; Connecting flexible pipe 23 is distributed on the outer peripheral face of tumbler 13; And be connected with the internal cavities of filtering table 16, steam-water separator 21 be connected flexible pipe 23 and connect, vavuum pump 22 is connected with steam-water separator 21.The vavuum pump 22 of vacuum system continues constant negative pressure for the filtering table 16 of host computer system provides, and the solid particle in the slurries that the FGD system produces can be adsorbed onto on the surface of filtering table 16, forms filter cake, and continues filter cake is aspirated.Steam-water separator 21 is used for separating with gas enter into the moisture that connects flexible pipe 23 through filtering table 16, avoids moisture to be drawn into vavuum pump 22 in a large number, and influences the use of vavuum pump 22.
Filtering table 16 is after work a period of times, and the micropore on the filtering table 16 can stop up because of fouling, can reduce filter efficiency, and purging system is the device of cleaning that is used to guarantee filtration continuation and the slurry tank 12 of filtering table 16.This purging system comprises agitating device 31, ultrasonic cleaning equipment 32, back purge system and chemically-cleaning device; Agitating device 31 is generally pendulum rake formula; It is connected with the stirring decelerator through one group of swing arm linkage; Stir decelerator driving swing arm linkage and in slurry tank 12, move, to guarantee that slurries can not precipitate in the course of the work.Ultrasonic cleaning equipment 32 is arranged in the slurry tank 12, and it utilizes cavitation effect and the decay very little characteristic of ultrasonic wave in liquid, to filtering table 16 surfaces, internal cavities, with and the micropore on surface effectively clean.Back purge system comprises electric control valve 331, Pressure gauge 332 and buffer 333; This back purge system is connected with filtering table 16 inner cavitys through pipeline; During operate as normal, back purge system is passed to clean water in the inner cavity of filtering table 16, the cleaning that filtering table 16 is carried out from inside to outside.Chemically-cleaning device is connected with back purge system; Chemically-cleaning device comprises acid solution jar 341 and measuring pump 342; Measuring pump 342 is pumped into acid solution in the pipeline of back purge system; To the micropore of filtering table 16 with and internal cavities on scale formation eliminate, make micropore unimpeded, guarantee that the strainability of filtering table 16 continues reliable.Purging system adopts Chemical cleaning and ultrasonic waves for cleaning dual mode to mix and cleans; Ultrasonic waves for cleaning and Chemical cleaning can be carried out simultaneously; Wherein, The Chemical cleaning mode is to adopt a kind of chemical reagent that the dirt that fouling produces is permeated, dissolve, and then the shock wave through ultrasonic cavitation effect generation with filtering table 16 internal cavities with and the dirt of surface micropore peel off.
The control system controls each drive motors in host computer system, vacuum system and the purging system of entire equipment, valve etc., and it is connected with host computer system, comes the on off state of main control system system; The control system is connected with vacuum system, in order to the on off state of control vacuum system; The control system is connected with purging system, is used to control the on off state of purging system.This control system comprises PLC controller and first liquid level sensor that is connected with this PLC controller, second liquid level meter, vacuum transducer and ultrasonic power etc.; Wherein, First liquid level sensor is installed in the slurry tank 12; The vacuum transducer and second liquid level sensor are installed on the steam-water separator 21, and ultrasonic power is connected with ultrasonic cleaning equipment 32.
During the work of the utility model smoke-gas wet desulfurization gypsum rotating disk dewaterer; Evenly get into slurry tank 12 bottoms through the slurries on the slurry tank 12 by feed pipe 121; The control of control system drives reduction box 142 and drives tumbler 13 rotations with drive motors 141; Filtering table 16 is along with tumbler 13 rotates, and experiences pulp absorbing area, filtering area, drip washing district, dry section, discharge zone and backwash district successively, and control device control vacuum system is opened; Vacuum system is that filtering table 16 internal cavities provide lasting constant negative pressure; Solid particle in the slurries is adsorbed on filtering table 16 surfaces through the micropore on the filtering table 16, and arriving the device for discharging position, is unloaded by device for discharging.In said process, when slurries reached the appointment liquid level, first fluid level controller was sent to the PLC controller with signal, under the control of PLC controller, and the valve open on the spout hole 123, unnecessary slurries flow out.Filtering table is after 16 work a period of times, and the micropore on the filtering table 16 can stop up because of fouling, can reduce filter efficiency, therefore needs to open purging system equipment is cleaned.Before opening Chemical cleaning and ultrasonic waves for cleaning; Control system main control system system-down, and the valve open on the control plasma discharge hole 122 drain the slurries in the slurry tank 12 only; Then; Valve open on the control system control rinse mouth 124 washes slurry tank 12 usefulness clear water, and closes plasma discharge hole 122.After the clear water in the slurry tank 12 arrives the precalculated position; First liquid level sensor reaches the PLC controller with signal; PLC controller control wave cleaning device 32, back purge system and chemically-cleaning device are opened, and the micropores on the internal cavities of slurry tank 12, filtering table 16 and filtering table surface, filtering table 16 surfaces are cleaned.
The filtering table 16 of the utility model smoke-gas wet desulfurization gypsum rotating disk dewaterer can adopt disc that white fused alumina ceramic wafer or volcanic rock process as its filter medium; Can also adopt other media such as filter cloth or screen cloth to process; Its shape can be the annular plate-like, also can be other ring discoid; The plasma discharge mode of slurry tank 12 can adopt high-order from row's mode, the mode that also can adopt the zero-bit pump to take out; Agitating device 31 in the purging system can also adopt the mode of air supporting stirring except adopting above-mentioned churned mechanically form.
The above is merely the preferred embodiment of the utility model, and is in order to restriction the utility model, not all within the spirit and principle of the utility model, any modification of being done, is equal to replacement, improvement etc., all should be included within the protection domain of the utility model.
Claims (8)
1. smoke-gas wet desulfurization gypsum rotating disk dewaterer; It is characterized in that: comprise host computer system and vacuum system, said host computer system comprises frame, slurry tank, tumbler, drive unit, device for discharging and filtering table, and the two ends of said slurry tank are fixed on the said frame; Said tumbler is a cylindrical structural; Its two ends are fixed on the two ends of said slurry tank, and said drive unit drives said tumbler and in said slurry tank, rotates, and said tumbler is provided with a plurality of said filtering tables; Said filtering table is a ring discoid; Each filtering table is all around on the outer circumference surface that is arranged on said tumbler, and said filtering table inside has cavity, on the surface of said filtering table, is provided with the micropore that is connected with said cavity; Said device for discharging is fixed on the said slurry tank, and contacts with the surface of said filtering table; Said vacuum system is connected with the inner cavity of said filtering table.
2.
2.A kind of smoke-gas wet desulfurization gypsum rotating disk dewaterer according to claim 1; It is characterized in that: said vacuum system comprises steam-water separator, vavuum pump and is connected flexible pipe; Said connection flexible pipe is distributed on the outer peripheral face of said tumbler; And be connected with the internal cavities of said filtering table, said steam-water separator connects with the said flexible pipe that is connected, and said vavuum pump is connected with said steam-water separator.
3. a kind of smoke-gas wet desulfurization gypsum rotating disk dewaterer according to claim 2 is characterized in that: also comprise purging system; Said purging system comprises agitating device, ultrasonic cleaning equipment, back purge system and chemically-cleaning device; Said agitating device and said ultrasonic cleaning equipment all are arranged in the said slurry tank; Said chemically-cleaning device is connected with said back purge system, and said back purge system is connected with the inner cavity of said filtering table through pipeline.
4. a kind of smoke-gas wet desulfurization gypsum rotating disk dewaterer according to claim 3 is characterized in that: said agitating device is that device is mixed in mechanical stirring device or gas mixing.
5. a kind of smoke-gas wet desulfurization gypsum rotating disk dewaterer according to claim 4; It is characterized in that: said mechanical stirring device comprises the swing arm linkage and stirs decelerator that said stirring decelerator drives said swing arm linkage and in said slurry tank, moves.
6. a kind of smoke-gas wet desulfurization gypsum rotating disk dewaterer according to claim 3 is characterized in that: also comprise the control system; Said control system is connected with said host computer system, is used to control the on off state of said host computer system; Said control system is connected with said vacuum system, in order to control the on off state of said vacuum system; Said control system is connected with said purging system, is used to control the on off state of said purging system.
7. according to each described a kind of smoke-gas wet desulfurization gypsum rotating disk dewaterer of claim 1 to 6, it is characterized in that: the disc that said filtering table employing capillary ceramic plate, volcanic rock are processed is as its filter medium.
8. according to each described a kind of smoke-gas wet desulfurization gypsum rotating disk dewaterer of claim 1 to 6, it is characterized in that: the bottom of said slurry tank is provided with charging void channels and plasma discharge hole, on the sidewall of said slurry tank, is provided with spout hole.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204488533U CN202315515U (en) | 2011-11-14 | 2011-11-14 | Flue gas wet flue gas desulfurization gypsum rotary table dehydrator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204488533U CN202315515U (en) | 2011-11-14 | 2011-11-14 | Flue gas wet flue gas desulfurization gypsum rotary table dehydrator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202315515U true CN202315515U (en) | 2012-07-11 |
Family
ID=46427517
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011204488533U Withdrawn - After Issue CN202315515U (en) | 2011-11-14 | 2011-11-14 | Flue gas wet flue gas desulfurization gypsum rotary table dehydrator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202315515U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102430276A (en) * | 2011-11-14 | 2012-05-02 | 烟台桑尼核星环保设备有限公司 | Wet flue gas desulfurization gypsum dehydrator |
| CN103394224A (en) * | 2013-05-02 | 2013-11-20 | 杭州蓝轩环保科技有限公司 | Scraper system of disc type dehydration machine |
| CN105268235A (en) * | 2015-11-08 | 2016-01-27 | 杭州蓝轩环保科技有限公司 | Filtering plate, vertical rotation gypsum dehydrator, working method and gypsum dehydrating system |
-
2011
- 2011-11-14 CN CN2011204488533U patent/CN202315515U/en not_active Withdrawn - After Issue
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102430276A (en) * | 2011-11-14 | 2012-05-02 | 烟台桑尼核星环保设备有限公司 | Wet flue gas desulfurization gypsum dehydrator |
| CN102430276B (en) * | 2011-11-14 | 2015-03-04 | 烟台桑尼核星环保设备有限公司 | Wet flue gas desulfurization gypsum dehydrator |
| CN103394224A (en) * | 2013-05-02 | 2013-11-20 | 杭州蓝轩环保科技有限公司 | Scraper system of disc type dehydration machine |
| CN103394224B (en) * | 2013-05-02 | 2015-11-18 | 杭州蓝轩环保科技有限公司 | A kind of doctor blade system of disc type dewaterer |
| CN105268235A (en) * | 2015-11-08 | 2016-01-27 | 杭州蓝轩环保科技有限公司 | Filtering plate, vertical rotation gypsum dehydrator, working method and gypsum dehydrating system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102430276B (en) | Wet flue gas desulfurization gypsum dehydrator | |
| CN202497759U (en) | Sewage filtering device without requiring shutdown | |
| CN202315515U (en) | Flue gas wet flue gas desulfurization gypsum rotary table dehydrator | |
| US20180370828A1 (en) | Membrane bioreactor for strengthening membrane fouling control and method thereof | |
| CN207591408U (en) | Sewage treating machine | |
| CN108126403A (en) | A kind of sewage treating machine | |
| CN105289084A (en) | Disc dehydrator | |
| CN103933768A (en) | Self-cleaning filter | |
| CN104056481A (en) | Double-helix rotary plate vacuum filter | |
| CN209092849U (en) | A kind of environment protection energy-saving efficient plate chain type ceramic filter | |
| CN204798946U (en) | Full -automatic back flush filter of steady voltage | |
| CN205461280U (en) | Novel filter cloth disc hydroextractor | |
| CN112607919A (en) | Layered sewage treatment equipment | |
| CN205308850U (en) | Plug / aluminium lid cleaning machine | |
| CN207654895U (en) | A kind of mine cleaner for not shutting down cleaning dust | |
| CN208249904U (en) | A kind of Purification of Carbon Nanotubes equipment | |
| CN110180491A (en) | A kind of Waste water treatment adsorbent and its preparation and regeneration method | |
| CN205235548U (en) | Disc hydroextractor | |
| CN105776513B (en) | A kind of membrane bioreactor and its operation method for reinforcing control membrane fouling | |
| CN102080044B (en) | Discharging mechanism of straw discharge cleaning on upper part of straw methane anaerobic tank | |
| CN201676604U (en) | Pressure-bearing automatic blowdown filter | |
| CN107986307A (en) | A kind of vacuum type filtration apparatus that turns over for the production of red mud alumina by sintering | |
| CN211357927U (en) | Farmland drainage filter equipment | |
| CN204601909U (en) | A kind of high-efficiency dust remover for industry | |
| CN208648962U (en) | A kind of liquor production wastewater treatment equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20120711 Effective date of abandoning: 20150304 |
|
| RGAV | Abandon patent right to avoid regrant |