CN204563860U - Water-bath rotating the needle method dust purifier - Google Patents

Water-bath rotating the needle method dust purifier Download PDF

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CN204563860U
CN204563860U CN201520252927.4U CN201520252927U CN204563860U CN 204563860 U CN204563860 U CN 204563860U CN 201520252927 U CN201520252927 U CN 201520252927U CN 204563860 U CN204563860 U CN 204563860U
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rotating
liquid
dust
needle
groove body
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李焱
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Abstract

Water-bath rotating the needle method dust purifier disclosed in the utility model, comprise support, liquid holding groove body is placed with in frame bottom, blow-off pipe is connected with bottom described liquid holding groove body, liquid holding groove body is placed with some ventilative orifice plates side by side, one purification chamber is all installed above each ventilative orifice plate, control of dust cannelure is connected with at purification top of chamber, described control of dust cannelure bottom surface has dirt liquid floss hole, dust discharge liquid sealing pipe is connected with at described dirt liquid floss hole place, described dust discharge liquid sealing pipe lower end is inserted in liquid holding groove body groove, rotating the needle wheel is installed in described control of dust cannelure, described rotating the needle wheel is fixed on motor output shaft end.The utility model ash-laden gas passes ventilative orifice plate aperture from bottom to top with certain flow rate, undercoating liquid district, bubbling area, up forming splash district, the splash risen is by High Rotation Speed many pin interceptions radially, cutting, collision, drop laying dust is adsorbed, and rotating the needle wheel can form the rotational field of unified angular speed in rotary course.

Description

Water-bath rotating the needle method dust purifier
Technical field
The utility model relates to a kind of purification treatment device for smoke dust, is specifically related to a kind of water-bath rotating the needle method dust purifier.
Background technology
Coal-fired Thermal Power boiler and industrial furnace cellar for storing things, the flue gas of discharging, although have passed through the dedusting of the dry collector such as pocket type or electrostatic, but still have the dustiness of tens milligrams/cubic metre, total amount is huge, the gypsum rain especially also having wet desulphurization to produce, the SO3 etc. of water smoke and escape, be discharged in air, the generation of haze is had a significant impact, threatens the healthy of people, therefore need to do further purified treatment.Traditional dry collector cannot overcome the above problems, although wet scrubber can except the grit of lower more than 0.1um, purification efficiency is relatively high, but traditional wet scrubber mainly contains wet cottrell and Washing dust remover, and wet cottrell has started application in indivedual apparatus of thermo-electric power boiler gas cleaning, but, complex structure, involve great expense, operation and maintenance cost is high, conventional washing formula deduster, its vapor-liquid separating structure is passive type substantially, some water smoke is separated not get off, and resistance is large, consume energy high, according to rotary filter net disk structure, during the sticking gypsum rain of separating belt, meeting control of dust in its wheel rim frame, or be adsorbed on filter screen silk, not easy to clean, and separating effect can be made to be deteriorated.
Utility model content
The purpose of this utility model is for the technical problem such as cleaner complex structure, dust removing effects in prior art be not good, a kind of water-bath rotating the needle method dust purifier is provided, this clearing machine structure is simple, manufacturing cost is low, energy consumption is low, water saving, high to purification efficiencies such as dust particale, water smoke, gypsum mist and SO3, working service is convenient, long working life.
Technical scheme: a kind of water-bath rotating the needle method dust purifier, comprise support, liquid holding groove body is placed with in frame bottom, at cradle top, brace summer is installed, brace summer is placed with lamina tecti, lamina tecti is vertically provided with motor, blow-off pipe is connected with bottom described liquid holding groove body, liquid holding groove body is placed with some ventilative orifice plates side by side, liquid is loaded with in described liquid holding groove body, liquid covers ventilative orifice plate, form fluid zone, one purification chamber is all installed above each ventilative orifice plate, control of dust cannelure is connected with at purification top of chamber, described control of dust cannelure bottom surface has dirt liquid floss hole, dust discharge liquid sealing pipe is connected with at described dirt liquid floss hole place, described dust discharge liquid sealing pipe lower end is inserted in liquid holding groove body groove, rotating the needle wheel is installed in described control of dust cannelure, described rotating the needle wheel is fixed on motor output shaft end.
Based on technique scheme, described rotating the needle wheel by least one deck radially, the dials of the even isometric layout of spininess fixedly formed by fixed cover after vertically being suppressed by welding or adhesive, fixed cover is fixedly set in motor output shaft end.
Based on technique scheme, described ventilative orifice plate is provided with liquid supplementation pipe, in liquid holding groove body groove, is placed with fluid level measuring instrument, described liquid supplementation pipe is provided with magnetic valve, magnetic valve is connected with liquid level controller by wire, and described liquid level controller is connected with fluid level measuring instrument through wire.
Based on technique scheme, described control of dust cannelure cross section is in " C " font, and take turns position relative with rotating the needle, and described control of dust cannelure lower port diameter is less than rotating the needle and takes turns external diameter, back cut diameter is greater than rotating the needle wheel external diameter, and control of dust cannelure groove inner height is greater than rotating the needle wheel vertical height.
Based on technique scheme, described liquid holding groove body is designed to " well " font groove, and groove bottom is inclined-plane, and blow-off pipe is positioned at inclined-plane lowest part.
Based on technique scheme, described purification chamber is up-narrow and down-wide trapezoidal container.
Based on technique scheme, the angle of described rotating the needle wheel between the adjacent needles of same layer dials is 2-3 °.
Based on technique scheme, described brace summer is the brace summer of falling T-shape.
Based on technique scheme, 2/3 position from top to bottom to be inserted in liquid holding groove body groove in described dust discharge liquid sealing pipe lower end.
Based on technique scheme, described ventilative orifice plate is square plate, plate body is evenly arranged some apertures, aperture that centre-to-centre spacing is consistent.
The beneficial effects of the utility model: 1, because arranging ventilative orifice plate, maintenance one liquid level on it, under suction function, ash-laden gas is with certain flow rate from bottom to top through ventilative orifice plate aperture, and undercoating liquid district, produces bubble, and bubble coalescence forms bubbling area ,up forming splash district, large drop falls, droplet is brought to rotating the needle wheel by air-flow, because bubble provides huge gas-liquid contact surface, and this surface merges at air-flow, increases, constantly update in the violent process that formed again of breaking, provide the grit making to carry secretly in gas and collide the condition be attached on liquid film, reach the effect of grit in water-bath washing adsorbed gas.
2, because arranging rotating the needle wheel, in its rotary course, the splash of rising is by High Rotation Speed many pin interceptions radially, cutting, collision, and drop laying dust is adsorbed, the vortex flow field of unified angular speed can be formed in rotary course, under its centrifugal action, dirt liquid is easy to be thrown in control of dust cannelure, is separated when obtaining pole, purified gas is discharged from the upper end that rotating the needle is taken turns, because pin is arranged radially, without dead angle control of dust, therefore without the need to cleaning.
3, because arranging control of dust cannelure, avoid splash decline dirt without rotating the needle wheel and directly discharge, meanwhile, ensure that the drop and micronic dust throwing to its wall is adsorbed and can not be taken away by air-flow.
4, because arranging liquid sealing pipe, the dirt liquid that control of dust cannelure is separated can drain in the groove of liquid holding groove body in time, due to certain depth in the insertion groove of liquid sealing pipe lower end, is sealed by liquid, and therefore dirt liquid can flow down and gas enters not go.
5, because arranging liquid controller, make the liquid level height on ventilative orifice plate controllable, after setting liquid level, during lower than low level setting value, fluid infusion opened by magnetic valve, stops fluid infusion higher than during high-order setting value.
6, because arranging liquid holding groove body, its intersecting parallels groove ramped bottom surface, is convenient to dirt liquid and discharges toward lower sedimentation, intersecting parallels groove is connected, not only make cell body intensity increase, become installation multiple stage water-bath rotating the needle method dust purifier simultaneously and provide public basic part, to meet the occasion of different flue gas flow.
Accompanying drawing explanation
Fig. 1 is the utility model water-bath rotating the needle method clarifying smoke owner TV structure schematic diagram;
Fig. 2 is the utility model water-bath rotating the needle method dust purifier plan structure schematic diagram;
Fig. 3 is ventilative orifice plate plan structure schematic diagram;
Fig. 4 is ventilative orifice plate cross-sectional view;
Fig. 5 is that main TV structure schematic diagram taken turns by rotating the needle;
Fig. 6 is rotating the needle wheel plan structure schematic diagram;
Fig. 7 is the main TV structure schematic diagram of liquid holding groove body;
Fig. 8 is liquid holding groove body plan structure schematic diagram.
Number in the figure, 1 is liquid holding groove body, and 2 is ventilative plate hole, and 3 is dust discharge liquid sealing pipe, and 4 is control of dust ring shaped slot, and 41 is notch under control of dust cannelure, and 42 is notch on control of dust ring shaped slot, and 5 is purification chamber; 6 is rotating the needle wheel, and 7 is motor, and 8 is lamina tecti, and 9 is the brace summer of falling T-shape, and 10 is fluid level measuring instrument; 11 is liquid level controller, and 12 is liquid supplementation pipe, and 13 is magnetic valve, and 14 is inlet, and 15 is liquid level face; 16 is splash, and 17 is bubble, and 18 is blow-off pipe, and 19 is gas flow, and 20 is pin, and 21 is fixed cover, and 22 is adhesive, and 23 is compression plate.
Detailed description of the invention
Below in conjunction with detailed description of the invention, the utility model is described further, better to understand technical solutions of the utility model.
Embodiment 1: a kind of water-bath rotating the needle method dust purifier, see Fig. 1 and Fig. 2, comprise frame, at cradle top, the brace summer of falling T-shape 9 is installed, brace summer 9 is placed with lamina tecti 8, lamina tecti 8 is vertically provided with motor 7, described motor 7 output shaft is passed down through lamina tecti, liquid holding groove body 1 is placed with in frame bottom, as Fig. 7, shown in Fig. 8, liquid holding groove body 1 is designed to " well " font groove, groove bottom is inclined-plane, be convenient to heavy liquid toward lower sedimentation, discharge, on inclined-plane, lowest part is connected with blow-off pipe, " well " font groove, cell body intensity is not only made to increase, provide public basic part for installing multiple stage water-bath rotating the needle method smoke purifying equipment simultaneously.Described liquid holding groove body 1 is placed with a ventilative orifice plate 2, and as shown in Figures 3 and 4, described ventilative orifice plate is square plate, plate body is evenly arranged some apertures, aperture that centre-to-centre spacing is consistent.Aperture is evenly arranged, and is convenient to dust suction even, good purification.Liquid is loaded with in described liquid holding groove body 1, liquid covers ventilative orifice plate, form fluid zone, specifically see the liquid level face 15 shown in Fig. 1, ventilative orifice plate 2 is provided with liquid supplementation pipe 12, described liquid supplementation pipe 12 is provided with magnetic valve 13, magnetic valve 13 is connected with liquid level controller 11 by wire, liquid level controller 11 is connected with fluid level measuring instrument 10 through wire, described fluid level measuring instrument 11 is fixed in liquid holding groove body 1 groove, the installation of fluid level control device and liquid supplementation pipe, make the liquid level height on ventilative orifice plate 2 controllable, fluid zone is remained at and covers in ventilative orifice plate 2 certain altitude, enough bubbles can be formed after making ash-laden gas pass fluid zone, for later bubbling area ,splash district lays the first stone, to ensure purifying and dedusting effect.
Above ventilative orifice plate 2, by flange, purification chamber 5 is installed, described purification chamber 5 is a up-narrow and down-wide trapezoidal dirt liquid purifying vessel, and this purification cavity configuration design form, makes ash-laden gas in uphill process, volume reduces gradually, is convenient to splash and moves toward rotating the needle wheel place.Be connected with control of dust cannelure 4 at purification top, chamber 5, control of dust cannelure 4 avoids the splash dirt that declines and directly discharges affect purification efficiency without rotating the needle wheel, ensure that gas purification coefficiency.Rotating the needle wheel 6 is installed in control of dust cannelure 4, described control of dust cannelure 4 cross section is in " C " font, and with rotating the needle, to take turns 6 positions relative, control of dust cannelure 4 end opening 41 diameter is less than rotating the needle and takes turns 6 external diameters, 42 diameters suitable for reading are greater than rotating the needle and take turns 6 external diameters, and control of dust cannelure 4 groove inner height is greater than rotating the needle and takes turns 6 vertical height.As shown in Figures 5 and 6, described rotating the needle wheel 6 by 4 layers radially, the dials of the even isometric layout of spininess is by after adhesive 22 vertically compacting, overall being fixed together by fixed cover 21 is formed again, compression plate 21 is installed bottom fixed cover 21, upwards held out against by bottom by compression plate 23, make to join between adjacent dials tightr, tight, fixed cover 21 is fixedly set in motor 7 output shaft end.Angle between same layer dials adjacent needles 20 is 2-3 °, each pin identical length etc.Described pin be the corrosion-resistant wire rod of stainless steel after heat treatment, good rigidity and toughness can be reached.The present embodiment arranges rotating the needle wheel, in its rapid rotary course, the splash of rising or micronic dust is made to be collided by the pin that upper many radial layouts taken turns by rotating the needle, cut, adsorb on the one hand, throw on control of dust cannelure inwall along pin, define the rotational field of unified angular speed on the other hand, strengthen dirt liquid by the effect thrown on control of dust cannelure inwall, the micronic dust of separable more than 0.1um, separating effect is splendid.The dirt liquid separated for making control of dust cannelure can drain in the groove of liquid holding groove body in time, dirt liquid floss hole is had in control of dust cannelure 4 bottom surface, at dirt liquid floss hole, place is connected with dust discharge liquid sealing pipe 3, dust discharge liquid sealing pipe 3 lower end is inserted in liquid holding groove body 1 groove, and insert certain depth, preferably 2/3 position from top to bottom to groove.Due to certain depth in the insertion groove of liquid sealing pipe lower end, sealed by liquid, therefore dirt liquid can flow down and gas enters not go.
The present embodiment specific works process is as follows: ash-laden gas is with certain flow rate from bottom to top through ventilative orifice plate 2 aperture, and through fluid zone, produce bubble 17, bubble coalescence forms bubbling area ,up forming splash 16, concrete label 19 gas flow as shown in Figure 1, now, large drop falls, and droplet is brought to rotating the needle wheel by air-flow, and the splash of rising is by High Rotation Speed many pin interceptions radially, cutting, collision; Because bubble provides huge gas-liquid contact surface, and this surface merges at air-flow, increases, constantly update in the violent process that formed again of breaking, provide the grit making to carry secretly in gas and collide the condition be attached on liquid film, therefore drop laying dust is easy to be adsorbed.The drop laying dust be blocked is under centrifugal action, be easy to be thrown in control of dust cannelure 4, be separated in time, the dirt liquid separated from control of dust cannelure can drain in the groove of liquid holding groove body in time, purified gas is discharged from rotating the needle wheel top, meanwhile, liquid controller regulates the liquid level height on ventilative orifice plate in time, after setting liquid level, during lower than low level setting value, magnetic valve is opened, and liquid supplementation pipe, from inlet 14 fluid infusion, stops fluid infusion higher than during high-order setting value.Ensure that liquid level height in the reasonable scope.Thus ensure high-precision depuration quality.The present embodiment structure is simple, low cost of manufacture, and purification efficiency is high, and working service is convenient, long working life.
Finally it should be noted that: above-described embodiment is only explanation technical solutions of the utility model; and non-limiting the utility model protection domain; the utility model can install the water-bath rotating the needle method smoke purifying equipment of multi-machine parallel connection on " well " font liquid holding groove body according to different flue gas flow occasion; and only a set of smoke purifying equipment that than the above-mentioned ones limits; all employings are similar to technical solutions of the utility model or only make the technical scheme of equivalent transformation, all belong to the utility model protection domain.

Claims (10)

1. a water-bath rotating the needle method dust purifier, comprise support, it is characterized in that: be placed with liquid holding groove body in frame bottom, at cradle top, brace summer is installed, brace summer is placed with lamina tecti, lamina tecti is vertically provided with motor, blow-off pipe is connected with bottom described liquid holding groove body, liquid holding groove body is placed with some ventilative orifice plates side by side, liquid is loaded with in described liquid holding groove body, liquid covers ventilative orifice plate, form fluid zone, one purification chamber is all installed above each ventilative orifice plate, control of dust cannelure is connected with at purification top of chamber, described control of dust cannelure bottom surface has dirt liquid floss hole, dust discharge liquid sealing pipe is connected with at described dirt liquid floss hole place, described dust discharge liquid sealing pipe lower end is inserted in liquid holding groove body groove, rotating the needle wheel is installed in described control of dust cannelure, described rotating the needle wheel is fixed on motor output shaft end.
2. water-bath rotating the needle method dust purifier according to claim 1, it is characterized in that: described rotating the needle wheel by least one deck radially, the dials of the even isometric layout of spininess fixedly formed by fixed cover after vertically being suppressed by welding or adhesive, fixed cover is fixedly set in motor output shaft end.
3. water-bath rotating the needle method dust purifier according to claim 1, it is characterized in that: on described ventilative orifice plate, liquid supplementation pipe is installed, fluid level measuring instrument is placed with in liquid holding groove body groove, described liquid supplementation pipe is provided with magnetic valve, magnetic valve is connected with liquid level controller by wire, and described liquid level controller is connected with fluid level measuring instrument through wire.
4. water-bath rotating the needle method dust purifier according to claim 1, it is characterized in that: described control of dust cannelure cross section is in " C " font, and with rotating the needle, to take turns position relative, described control of dust cannelure lower port diameter is less than rotating the needle wheel external diameter, back cut diameter is greater than rotating the needle wheel external diameter, and control of dust cannelure groove inner height is greater than rotating the needle wheel vertical height.
5. water-bath rotating the needle method dust purifier according to claim 1, is characterized in that: described liquid holding groove body is designed to " well " font groove, and groove bottom is inclined-plane, and blow-off pipe is positioned at inclined-plane lowest part.
6. water-bath rotating the needle method dust purifier according to claim 1, is characterized in that: described purification chamber is up-narrow and down-wide trapezoidal container.
7. water-bath rotating the needle method dust purifier according to claim 1, is characterized in that: the angle of described rotating the needle wheel between the adjacent needles of same layer dials is 2-3 °.
8. water-bath rotating the needle method dust purifier according to claim 1, is characterized in that: described brace summer is the brace summer of falling T-shape.
9. water-bath rotating the needle method dust purifier according to claim 1, is characterized in that: 2/3 position from top to bottom to be inserted in liquid holding groove body groove in described dust discharge liquid sealing pipe lower end.
10. the water-bath rotating the needle method dust purifier according to any one of claim 1-9, is characterized in that: described ventilative orifice plate is square plate, plate body is evenly arranged some apertures, aperture that centre-to-centre spacing is consistent.
CN201520252927.4U 2015-04-24 2015-04-24 Water-bath rotating the needle method dust purifier Active CN204563860U (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104785063A (en) * 2015-04-24 2015-07-22 李焱 Smoke dust purification machine adopting water-bath needle rotating method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104785063A (en) * 2015-04-24 2015-07-22 李焱 Smoke dust purification machine adopting water-bath needle rotating method

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