CN204429071U - A kind of high-effect desulfurizing tower - Google Patents
A kind of high-effect desulfurizing tower Download PDFInfo
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- CN204429071U CN204429071U CN201420793431.3U CN201420793431U CN204429071U CN 204429071 U CN204429071 U CN 204429071U CN 201420793431 U CN201420793431 U CN 201420793431U CN 204429071 U CN204429071 U CN 204429071U
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Abstract
The utility model relates to a kind of high-effect desulfurizing tower, tower body is divided into discharge opeing section from bottom to top, air inlet section, gas liquid reaction section, liquid input section, gas-liquid separation section, the lower end of discharge opeing section is connected with at the bottom of tower, bottom at the bottom of tower arranges the discharging tube be connected with leakage fluid dram, the air inlet pipe that tower body sidewall stretches into tower body inside is arranged through in air inlet section, gas liquid reaction section is divided into the lower packing section and upper packing section that are separated, the spray atomizer be connected with feed tube is set in liquid input section, feed tube stretches into the inside of tower body by tower body sidewall, the upper end of gas-liquid separation section is connected with tower top, the exhaust outlet at tower top top is connected with blast pipe by eddy flow chamber, the bottom in eddy flow chamber arranges spiral board, the utility model has the advantages such as desulfurized effect is good, Liquid Flow is smooth and easy, gas-liquid separation is thorough, equipment good corrosion resistance, meets its application in fields such as oil, coal, chemical industry, pharmacy, environmental protection.
Description
Technical field
The utility model belongs to flue gas desulfurization technique field, relates to the dynamical desulfurizing tower that a kind of desulfurized effect is good.
Background technology
According to the World Health Organization and United Nations Environment Programme's statistics, annual that manufactured by the mankind, sulfurous fuels burning and exhausting is to the sulfur dioxide in air up to about 200,000,000 tons at present, and heavy damage atmospheric environment, governs the development of World Economics.Desulfurization just becomes one of important method solving contradiction between air pollution and economic development instantly.At present, in the sweetening process in the fields such as oil, coal, chemical industry, pharmacy, environmental protection, desulfurizing tower (also known as packed tower) is widely used.Therefore, the design of desulfurizing tower is vital to efficiently carrying out sweetening process.
In the desulfurizing tower of present application, doctor solution enters in tower above tower body, and after the sulfurous gas haptoreaction of the rising entered from below in tower, the gas after desulfurization is directly discharged outside tower.Existing desulfurizing tower in use can produce some problems, and then affect desulfurized effect, be specially: the air inlet of existing desulfurizing tower air inlet pipe directly sprays tower wall corresponding thereto, wash away phenomenon comparatively serious, accelerate the corrosion of tower wall, air inlet position easily produces secondary salt crystallization simultaneously, causes airflow fluctuation in tower, affects desulfurized effect; The carbon steel material of existing desulfurizing tower feed tube is comparatively vulnerable to the corrosion of doctor solution, and the spray atomizing effect of inlet is bad, makes contact area between gas phase and liquid phase less, and desulphurization reaction can not fully carry out, and affects desulfurized effect; In use there is comparatively serious packing support plate blockage problem in existing desulfurizing tower, make gas to be desulfurization to increase smoothly, doctor solution decline process is hindered, and affects desulfurized effect; In existing desulfurizing tower, because after haptoreaction, gas-liquid separation space is little, can carry more doctor solution secretly in processed gas, processed gas can produce comparatively serious corrosion to follow-up equipment after discharging.
Utility model content
The utility model technical issues that need to address are to provide a kind of high-effect desulfurizing tower, to solve the problems such as the desulfurized effect that existing desulfurizing tower in use occurs is poor, Liquid Flow has some setbacks, processed gas carries doctor solution secretly, equipment is perishable.
For solving the problems of the technologies described above, technical solution adopted in the utility model is:
A kind of high-effect desulfurizing tower, described desulfurizing tower comprises the tower body be arranged on base, described tower body comprises cylindrical tower body and is arranged at the bottom of the tower at tower body two ends and tower top, described tower body is divided into discharge opeing section from bottom to top, air inlet section, gas liquid reaction section, liquid input section, gas-liquid separation section, the lower end of described discharge opeing section is connected with at the bottom of tower, bottom at the bottom of described tower arranges the discharging tube be connected with leakage fluid dram, the air inlet pipe that tower body sidewall stretches into tower body inside is arranged through in described air inlet section, described gas liquid reaction section be divided into be separated support the lower packing section of filler by lower packing support plate and supported the upper packing section of filler by upper packing support plate, the spray atomizer be connected with feed tube is set in described liquid input section, described feed tube stretches into the inside of tower body by tower body sidewall, the upper end of described gas-liquid separation section is connected with tower top, the eddy flow chamber that the exhaust outlet at described tower top top arranges spiral board by bottom is connected with blast pipe.
Further improvement of the utility model is: described air inlet pipe is positioned at the end-enclosed of tower body and is arranged on the air inlet pipe supporting seat on tower body sidewall, arranges rectangle air inlet below the body of described air inlet pipe.
Further improvement of the utility model is: the grating type gripper shoe that described lower packing support plate is made up of grizzly bar and strip through hole; The hump formula gripper shoe that the hump formula projection that described upper packing support plate arranges circular through hole by surface forms.
Further improvement of the utility model is: described spray atomizer comprise be connected with feed tube be arranged on the spray chamber of tower body inside by atomizer bracing frame and be symmetricly set on the downward mist pipe of shower nozzle on spray chamber outer wall, the quantity of described mist pipe is 10 ~ 20, and the material of described spray atomizer is 304 stainless steels.
Further improvement of the utility model is: the height in described eddy flow chamber is 400 ~ 600 millimeters, diameter is 1400 ~ 1600 millimeters, the height of described spiral board is 50 ~ 70 millimeters, diameter is 1100 ~ 1300 millimeters, the windup-degree of the blade of described spiral board is 3 ~ 12 degree, described spiral board arranged outside is with the collecting tank of mozzle, and the lower end of described mozzle is fixedly installed on tower body sidewall.
Further improvement of the utility model is: described tower top and tower body sidewall are positioned at air inlet pipe, lower packing support plate, upper packing support plate top position arrange manhole.
Further improvement of the utility model is: tower body sidewall and the leakage fluid dram at described discharge opeing section two ends arrange liquid meter for measuring level of liquid port.
Further improvement of the utility model is: the tower body sidewall between described lower packing section and upper packing section arranges manometer port.
Further improvement of the utility model is: the tower body height of described desulfurizing tower is 30000 ~ 40000 millimeters, and the diameter of tower body is 3500 ~ 4500 millimeters.
Owing to have employed technique scheme, the technological progress acquired by the utility model is:
The high-effect desulfurizing tower of one of the present utility model, tower body height is 30000 ~ 40000 millimeters, the diameter of tower body is 3500 ~ 4500 millimeters, tower body is divided into discharge opeing section, air inlet section, gas liquid reaction section, liquid input section, gas-liquid separation section from bottom to top, specialized designs is carried out according to the function of every section, there is the advantages such as desulfurized effect is good, Liquid Flow is smooth and easy, gas-liquid separation is thorough, equipment good corrosion resistance, meet its application in fields such as oil, coal, chemical industry, pharmacy, environmental protection.Hydrogen sulfide in flue gas can be down to 3ppm by 1150ppm is de-by this desulfurizing tower.
The tower body sidewall at discharge opeing section two ends is arranged liquid meter for measuring level of liquid port, conveniently measure the height of doctor solution in discharge opeing section, can drain age velocity be controlled by discharging tube.
The tower body of air inlet section is arranged the air inlet pipe stretching into tower body inside, air inlet pipe is positioned at the end-enclosed of tower body, and the gas that can prevent air inlet from spraying is directly injected to the tower wall on opposite, causes comparatively serious washing away and the corrosion of accelerated tower wall to tower wall; Arrange rectangle air inlet below the body of air inlet pipe, the doctor solution of whereabouts can not produce secondary salt crystallization in air inlet position, and can not cause airflow fluctuation to the gas sprayed in air inlet, gas can enter desulfurizing tower inside stably; End is arranged on the air inlet pipe supporting seat on tower body sidewall, can play fixing and supporting role preferably to air inlet pipe.Sedimentation under the effect of the liquid that the dust in the gas entered can flow down in gas liquid reaction section is also flowed out from discharge opeing section along with liquid.
Gas liquid reaction section is made up of the packing section that two sections are separated, the lower packing support plate of lower packing section is grating type gripper shoe, grating type gripper shoe has strip through hole, pore cross-section is long-pending larger, the throughput of gas, liquid also increases relatively, can make that gas rises smoothly, liquid declines smoothly, and can not produce clogging, the width of through hole can strengthen, and makes liquid be easy to flow down and more even.The upper packing support plate of upper packing section is hump formula gripper shoe, it is protruding that hump formula gripper shoe surface arranges hump formula, free cross-sectional area is large, there is circular through hole simultaneously, for gas phase and liquid phase provide different circulation passages, thus avoid flowing interference therebetween, can make that gas rises smoothly, doctor solution declines smoothly, even if pressure drop is also very little under very high gas-liquid load, can also plays to gas phase and liquid phase fluid the effect of being uniformly distributed simultaneously, thus ensure efficient mass-transfer efficiency.Manometer port is set between two packing section, is beneficial to the gas pressure intensity in monitoring gas liquid reaction section.
The tower body of liquid input section is arranged the feed tube stretching into tower body inside, feed tube end arranges spray atomizer, enhance the spray atomizing effect of doctor solution, the doctor solution entering tower body inside is made to be dispersed into more tiny drop, the contact area between gas phase and liquid phase can be increased, desulphurization reaction is fully carried out; The shower nozzle of mist pipe is downward, avoids the doctor solution sprayed to be directly injected to Ta Bishang, causes comparatively serious washing away and the corrosion of accelerated tower wall to tower wall; Adopt 304 stainless steels, avoid the corrosion of doctor solution to spray atomizer.
By arranging eddy flow chamber and spiral board in gas-liquid separation section, effectively can carry out gas-liquid separation, first be that exhaust outlet is set at tower top medium position, increase the gas-liquid separation distance in gas uphill process and separated space, can reach between gas phase with liquid phase and be separated comparatively fully.Eddy flow chamber is set between exhaust outlet and blast pipe, eddy flow arranges spiral board in chamber, spiral board is arranged the blade with windup-degree, blade produces guiding and centrifugal action to the gas risen, the liquid carried secretly in gas can be got rid of Xiang Tabi, get rid of liquid gravitate afflux to tower wall to collecting tank, then flowed back in tower by mozzle.The windup-degree of the height of eddy flow chamber and spiral board and diameter, blade all produces material impact to the effect of gas-liquid separation, and the air resistance pressure drop through spiral board is no more than 0.05kPa, ensures that gas enters follow-up equipment smoothly.
Accompanying drawing explanation
Fig. 1 is three-dimensional structure diagram of the present utility model;
Fig. 2 is top view of the present utility model;
Fig. 3 is the A-A sectional view of the utility model Fig. 2;
Fig. 4 is the B-B sectional view of the utility model Fig. 2;
Fig. 5 is stereochemical structure exploded view of the present utility model;
Fig. 6 is the tower top partial enlarged drawing of the utility model Fig. 5;
Fig. 7 is the three-dimensional structure diagram of spiral board of the present utility model;
Fig. 8 is the top view of spiral board of the present utility model;
Fig. 9 is the C-C sectional view of Fig. 8 of the present utility model;
Figure 10 is the three-dimensional structure diagram of spray atomizer of the present utility model;
Figure 11 is the lower view of spray atomizer of the present utility model;
Figure 12 is the F-F sectional view of Figure 11 of the present utility model;
Figure 13 is the three-dimensional structure diagram of upper packing support plate of the present utility model;
Figure 14 is the top view of upper packing support plate of the present utility model;
Figure 15 is the E-E sectional view of Figure 14 of the present utility model;
Figure 16 is the three-dimensional structure diagram of lower packing support plate of the present utility model;
Figure 17 is the top view of lower packing support plate of the present utility model;
Figure 18 is the D-D sectional view of Figure 17 of the present utility model;
Figure 19 is the three-dimensional structure diagram of air inlet pipe of the present utility model;
Figure 20 is the lower view of air inlet pipe of the present utility model;
Figure 21 is the G-G sectional view of Figure 20 of the present utility model;
Wherein, 1, base, 2, at the bottom of tower, 2-1, leakage fluid dram, 3, tower body, 3-1, discharge opeing section, 3-2, air inlet section, 3-2-1, air inlet pipe supporting seat, 3-3, gas liquid reaction section, 3-3-1, lower packing section, 3-3-2, upper packing section, 3-4, liquid input section, 3-5, gas-liquid separation section, 4, tower top, 4-1, exhaust outlet, 5, discharging tube, 6, air inlet pipe, 6-1, air inlet, 7, lower packing support plate, 7-1, grizzly bar, 7-2, strip through hole, 8, upper packing support plate, 8-1, circular through hole, 8-2, hump formula is protruding, 9, feed tube, 10, spray atomizer, 10-1, spray chamber, 10-2, mist pipe, 10-2-1, shower nozzle, 10-3, atomizer bracing frame, 11, eddy flow chamber, 11-1, spiral board, 11-1-1, blade, 11-2, collecting tank, 11-3, mozzle, 12, blast pipe, 13, manhole, 14, liquid meter for measuring level of liquid port, 15, manometer port.
Detailed description of the invention
Below in conjunction with accompanying drawing, the utility model is described in further details.
The high-effect desulfurizing tower of one of the present utility model, comprises the tower body be arranged on base 1, tower body comprise cylindrical tower body 3 and to be arranged at the bottom of the tower at tower body 3 two ends 2 with tower top 4, specifically as shown in Figure 1.The tower body height of desulfurizing tower is 30000 ~ 40000 millimeters, and the diameter of tower body 3 is 3500 ~ 4500 millimeters.Tower body 3 is divided into discharge opeing section 3-1, air inlet section 3-2, gas liquid reaction section 3-3, liquid input section 3-4, gas-liquid separation section 3-5 from bottom to top, specifically sees shown in Fig. 3, Fig. 4, Fig. 5.
Discharge opeing section 3-1 is positioned at the lower end of tower body 3, the height of discharge opeing section 3-1 is 5000 ~ 5500 millimeters, tower body 3 sidewall at discharge opeing section 3-1 two ends and leakage fluid dram 2-1 arrange liquid meter for measuring level of liquid port one 4, the quantity of liquid meter for measuring level of liquid port one 4 is 4 ~ 6, the lower end of discharge opeing section 3-1 2 to be connected with at the bottom of tower, at the bottom of tower, the height of 2 is 1000 ~ 1200 millimeters, at the bottom of tower, the bottom of 2 arranges leakage fluid dram 2-1, leakage fluid dram 2-1 is connected with discharging tube 5, discharging tube 5 arranges measurement port for subsequent use, the quantity of measurement port for subsequent use is 1 ~ 4, outside the end protuberate basic unit 1 of discharging tube 5.Specifically see shown in Fig. 3, Fig. 4, Fig. 5.
Air inlet section 3-2 is positioned at the top of the discharge opeing section 3-1 of tower body 3, the height of air inlet section 3-2 is 2000 ~ 2500 millimeters, air inlet pipe 6 is set in air inlet section 3-2, it is inner that air inlet pipe 6 stretches into tower body 3 by tower body 3 sidewall, air inlet pipe 6 is positioned at the end-enclosed of tower body 3 and is arranged on air inlet pipe supporting seat 3-2-1, air inlet pipe supporting seat 3-2-1 is arranged on tower body 3 sidewall, the diameter of air inlet pipe 6 is 500 ~ 700 millimeters, rectangle air inlet 6-1 is set below the body of air inlet pipe 6, Open Side Down for air inlet 6-1, the length of air inlet 6-1 is 2500 ~ 2700 millimeters, width is 150 ~ 250 millimeters.Specifically see shown in Fig. 3, Fig. 5, Figure 19, Figure 20, Figure 21.
Gas liquid reaction section 3-3 is positioned at the top of the air inlet section 3-2 of tower body 3, the height of gas liquid reaction section 3-3 is 16500 ~ 17000 millimeters, gas liquid reaction section 3-3 is divided into the lower packing section 3-3-1 and upper packing section 3-3-2 that are separated, the height of two sections of packing section is 7500 ~ 8000 millimeters, the gap of 1000 ~ 1500 millimeters is had between two sections of packing section, tower body 3 sidewall between lower packing section 3-3-1 and upper packing section 3-3-2 arranges manometer port one 5, specifically sees shown in Fig. 3, Fig. 4, Fig. 5.Lower packing section 3-3-1 supports filler by lower packing support plate 7, and lower packing support plate 7 is grating type gripper shoes, is made up of, specifically sees shown in Figure 16, Figure 17, Figure 18 grizzly bar 7-1 and strip through hole 7-2; Upper packing section 3-3-2 supports filler by upper packing support plate 8, and upper packing support plate 8 is hump formula gripper shoes, and the protruding 8-2 of hump formula being arranged circular through hole 8-1 by surface forms, and specifically sees shown in Figure 13, Figure 14, Figure 15.The upper end of two sections of packing section all arranges filler cover plate.
Liquid input section 3-4 is positioned at the top of the gas liquid reaction section 3-3 of tower body 3, the height of liquid input section 3-4 is 2500 ~ 3000 millimeters, and arrange spray atomizer 10 in liquid input section 3-4, spray atomizer 10 is connected with feed tube 9, it is inner that feed tube 9 stretches into tower body 3 by tower body 3 sidewall, specifically as shown in Figure 6.Spray atomizer 10 comprises spray chamber 10-1, mist pipe 10-2, atomizer bracing frame 10-3, spray chamber 10-1 is connected with feed tube 9, spray chamber 10-1 is arranged on the inside of tower body 3 by atomizer bracing frame 10-3, the outer wall of spray chamber 10-1 is symmetrical arranged mist pipe 10-2, mist pipe 10-2 arranges the shower nozzle 10-2-1 that Open Side Down, the shower nozzle 10-2-1 of mist pipe 10-2 end is disposed on the same plane and circumferentially symmetrical, mist pipe 10-2 is arranged on upper end position and the medium position of spray chamber 10-1 sidewall, the shower nozzle 10-2-1 be arranged on the mist pipe 10-2 of spray chamber 10-2 sidewall upper position is positioned in outer circumference, the shower nozzle 10-2-1 be arranged on the mist pipe 10-2 of spray chamber 10-2 sidewall medium position is positioned in inside circumference, center bottom spray chamber 10-1 arranges a mist pipe 10-2, shower nozzle 10-2-1 on this root mist pipe 10-2 is positioned on the center of circle of outer circumference and inside circumference, the quantity of mist pipe 10-2 is 10 ~ 20, specifically see Fig. 6, Figure 10, Figure 11, shown in Figure 12, the material of spray atomizer 10 is 304 stainless steels.
Gas-liquid separation section 3-5 is positioned at the upper end of tower body 3, the height of gas-liquid separation section 3-5 is 2000 ~ 2500 millimeters, gas-liquid separation section 3-5 is connected with tower top 4, the height of tower top 4 is 1000 ~ 1200 millimeters, the exhaust outlet 4-1 at tower top 4 top is connected with blast pipe 12 by eddy flow chamber 11, the height in eddy flow chamber 11 is 400 ~ 600 millimeters, diameter is 1400 ~ 1600 millimeters, the bottom in eddy flow chamber 11 arranges spiral board 11-1, the height of spiral board 11-1 is 50 ~ 70 millimeters, diameter is 1100 ~ 1300 millimeters, the windup-degree of the blade 11-1-1 of spiral board 11-1 is 3 ~ 12 degree, spiral board 11-1 arranged outside collecting tank 11-2, mozzle 11-3 is set in collecting tank 11-2, the lower end of mozzle 11-3 is fixedly installed on tower body 3 sidewall, specifically see Fig. 6, Fig. 7, Fig. 8, shown in Fig. 9.
Tower top 4 and tower body 3 sidewall are positioned at air inlet pipe 6, lower packing support plate 7, upper packing support plate 8, filler cover plate top position arrange manhole 13, specifically see shown in Fig. 3, Fig. 5.
The course of work of the present utility model is: gas to be desulfurization enters in desulfurizing tower by air inlet pipe 6, the gas to be desulfurization entered in tower rises along tower body 3, doctor solution enters in desulfurizing tower by feed tube 9, and disperse through spray atomizer 10, doctor solution gravitate after dispersion and declining, the gas to be desulfurization risen contacts at gas liquid reaction section 3-3 with the doctor solution of decline, the two is by the abundant reaction in lower packing section 3-3-1 with upper packing section 3-3-2, sulphur-containing substance in gas to be desulfurization is desulfurized liquid and goes out, doctor solution continues to drop to discharge opeing section 3-1 and discharges tower body 3 by discharging tube 5, gas after desulfurization continues to rise to gas-liquid separation section, the gas being entrained with doctor solution carries out gas-liquid separation at gas-liquid separation section 3-5 because of Action of Gravity Field, the gas rising to eddy flow chamber 11 is through the guiding of the blade 11-1-1 of spiral board 11-1 and centrifugal action, the liquid carried secretly in gas is got rid of Xiang Tabi, get rid of liquid gravitate afflux to tower wall to collecting tank 11-2, flow back in tower by mozzle 11-3 again, gas after abundant separating liquid then discharges tower body 3 by blast pipe 12.
Claims (9)
1. a high-effect desulfurizing tower, described desulfurizing tower comprises the tower body be arranged on base (1), described tower body comprises cylindrical tower body (3) and is arranged on (2) at the bottom of the tower at tower body (3) two ends and tower top (4), it is characterized in that: described tower body (3) is divided into discharge opeing section (3-1) from bottom to top, air inlet section (3-2), gas liquid reaction section (3-3), liquid input section (3-4), gas-liquid separation section (3-5), the lower end of described discharge opeing section (3-1) is connected with (2) at the bottom of tower, the bottom of (2) at the bottom of described tower arranges the discharging tube (5) be connected with leakage fluid dram (2-1), be arranged through tower body (3) sidewall in described air inlet section (3-2) and stretch into the inner air inlet pipe (6) of tower body (3), described gas liquid reaction section (3-3) be divided into be separated support the lower packing section (3-3-1) of filler by lower packing support plate (7) and supported the upper packing section (3-3-2) of filler by upper packing support plate (8), the spray atomizer (10) be connected with feed tube (9) is set in described liquid input section (3-4), described feed tube (9) stretches into the inside of tower body (3) by tower body (3) sidewall, the upper end of described gas-liquid separation section (3-5) is connected with tower top (4), the eddy flow chamber (11) that the exhaust outlet (4-1) at described tower top (4) top arranges spiral board (11-1) by bottom is connected with blast pipe (12).
2. the high-effect desulfurizing tower of one according to claim 1, it is characterized in that: described air inlet pipe (6) is positioned at the end-enclosed of tower body (3) and is arranged on the air inlet pipe supporting seat (3-2-1) on tower body (3) sidewall, arranges rectangle air inlet (6-1) below the body of described air inlet pipe (6).
3. the high-effect desulfurizing tower of one according to claim 1, is characterized in that: the grating type gripper shoe that described lower packing support plate (7) is made up of grizzly bar (7-1) and strip through hole (7-2); The hump formula gripper shoe that the hump formula projection (8-2) that described upper packing support plate (8) arranges circular through hole (8-1) by surface forms.
4. the high-effect desulfurizing tower of one according to claim 1, it is characterized in that: described spray atomizer (10) comprise be connected with feed tube (9) be arranged on the inner spray chamber (10-1) of tower body (3) by atomizer bracing frame (10-3) and be symmetricly set on the downward mist pipe (10-2) of shower nozzle (10-2-1) on spray chamber (10-1) outer wall, the quantity of described mist pipe (10-2) is 10 ~ 20, and the material of described spray atomizer (10) is 304 stainless steels.
5. the high-effect desulfurizing tower of one according to claim 1, it is characterized in that: the height of described eddy flow chamber (11) is 400 ~ 600 millimeters, diameter is 1400 ~ 1600 millimeters, the height of described spiral board (11-1) is 50 ~ 70 millimeters, diameter is 1100 ~ 1300 millimeters, the windup-degree of the blade (11-1-1) of described spiral board (11-1) is 3 ~ 12 degree, described spiral board (11-1) arranged outside is with the collecting tank (11-2) of mozzle (11-3), and the lower end of described mozzle (11-3) is fixedly installed on tower body (3) sidewall.
6. the high-effect desulfurizing tower of the one according to any one of claim 1 ~ 5, is characterized in that: described tower top (4) and tower body (3) sidewall are positioned at air inlet pipe (6), lower packing support plate (7), upper packing support plate (8) top position arrange manhole (13).
7. the high-effect desulfurizing tower of one according to claim 6, is characterized in that: tower body (3) sidewall and the leakage fluid dram (2-1) at described discharge opeing section (3-1) two ends arrange liquid meter for measuring level of liquid port (14).
8. the high-effect desulfurizing tower of one according to claim 6, is characterized in that: tower body (3) sidewall between described lower packing section (3-3-1) and upper packing section (3-3-2) arranges manometer port (15).
9. the high-effect desulfurizing tower of one according to claim 6, is characterized in that: the tower body height of described desulfurizing tower is 30000 ~ 40000 millimeters, and the diameter of tower body (3) is 3500 ~ 4500 millimeters.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420793431.3U CN204429071U (en) | 2014-12-16 | 2014-12-16 | A kind of high-effect desulfurizing tower |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420793431.3U CN204429071U (en) | 2014-12-16 | 2014-12-16 | A kind of high-effect desulfurizing tower |
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| CN204429071U true CN204429071U (en) | 2015-07-01 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201420793431.3U Expired - Fee Related CN204429071U (en) | 2014-12-16 | 2014-12-16 | A kind of high-effect desulfurizing tower |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104492241A (en) * | 2014-12-16 | 2015-04-08 | 河北英都气化有限公司 | High-efficiency desulfurizing tower |
| CN106215668A (en) * | 2016-09-27 | 2016-12-14 | 长春东狮科贸实业有限公司 | A kind of desulfurizing tower |
| CN109432929A (en) * | 2018-11-24 | 2019-03-08 | 天伟化工有限公司 | A kind of washing tail gas devices and methods therefor during the cyclone drying suitable for polyvinyl chloride resin |
| CN111097249A (en) * | 2020-01-10 | 2020-05-05 | 新疆海天祥瑞环保工程有限公司 | Rotational flow-based high-efficiency turbulent flow atomization mixing desulfurization dust removal process |
-
2014
- 2014-12-16 CN CN201420793431.3U patent/CN204429071U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104492241A (en) * | 2014-12-16 | 2015-04-08 | 河北英都气化有限公司 | High-efficiency desulfurizing tower |
| CN104492241B (en) * | 2014-12-16 | 2016-05-18 | 河北英都气化有限公司 | A kind of high-effect desulfurizing tower |
| CN106215668A (en) * | 2016-09-27 | 2016-12-14 | 长春东狮科贸实业有限公司 | A kind of desulfurizing tower |
| CN106215668B (en) * | 2016-09-27 | 2018-10-30 | 长春东狮科贸实业有限公司 | A kind of desulfurizing tower |
| CN109432929A (en) * | 2018-11-24 | 2019-03-08 | 天伟化工有限公司 | A kind of washing tail gas devices and methods therefor during the cyclone drying suitable for polyvinyl chloride resin |
| CN111097249A (en) * | 2020-01-10 | 2020-05-05 | 新疆海天祥瑞环保工程有限公司 | Rotational flow-based high-efficiency turbulent flow atomization mixing desulfurization dust removal process |
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