CN212713388U - Wet purification device for total sulfur removal of blast furnace gas - Google Patents

Wet purification device for total sulfur removal of blast furnace gas Download PDF

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CN212713388U
CN212713388U CN202021580345.6U CN202021580345U CN212713388U CN 212713388 U CN212713388 U CN 212713388U CN 202021580345 U CN202021580345 U CN 202021580345U CN 212713388 U CN212713388 U CN 212713388U
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tower
blast furnace
catalytic hydrolysis
furnace gas
water
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李鹏飞
朱迎新
孙健
程正霖
刘瑱
王广春
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Central Research Institute of Building and Construction Co Ltd MCC Group
MCC Energy Saving and Environmental Protection Co Ltd
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Central Research Institute of Building and Construction Co Ltd MCC Group
MCC Energy Saving and Environmental Protection Co Ltd
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Abstract

The utility model relates to a wet purification device for total sulfur removal of blast furnace gas, which comprises a catalytic hydrolysis tower, a desulfurizing tower and an auxiliary device; the blast furnace gas after dust removal and waste heat and residual pressure power generation sequentially passes through a catalytic hydrolysis tower and a desulfurization tower; organic sulfur such as carbonyl sulfur (COS) and carbon disulfide (CS2) is catalytically hydrolyzed in a catalytic hydrolysis tower and converted into hydrogen sulfide (H2S); water and an alkaline absorbent are sprayed into the desulfurizing tower through the process water tank, the alkali liquor storage tank and the feeding system to absorb hydrogen sulfide (H2S), sulfur dioxide (SO2), hydrogen chloride (HCl) and other acidic gases, SO that the removal of sulfur-containing substances in the blast furnace gas is realized, the problem that the sulfur dioxide (SO2) exceeds the standard is solved from the source, and meanwhile, the problem of corrosion of a gas pipeline is controlled to a certain extent by the synergistic removal of the hydrogen chloride (HCl).

Description

Wet purification device for total sulfur removal of blast furnace gas
Technical Field
The utility model relates to a wet purification device for total sulfur removal of blast furnace gas, in particular to a device capable of realizing COS and CS in blast furnace gas2、H2S、SO2A wet purification device for removing sulfur-containing substances and removing HCl in a synergistic manner belongs to the pollutant control technology in the technical field of environmental protection engineering, and is used for realizing total sulfur removal of blast furnace gas in a set of process.
Background
The blast furnace gas is used as the combustible gas with the maximum output of the steel enterprises, and the statistical output is up to 700-. The existing blast furnace gas purification and subsequent application mainly adopts bag type dust removal to remove particulate matters, and the particulate matters are sent to user units such as a blast furnace hot blast stove, a steel rolling heating furnace, gas power generation and the like to be used as fuels after TRT residual pressure power generation, but the blast furnace gas still contains harmful substances such as sulfur, chlorine and the like. With the promulgation of the opinion about the promotion of the ultra-low emission in the steel industry, the steel industry formally enters the 'ultra-low emission' era, and users of blast furnace hot blast stoves, steel rolling heating furnaces, gas power generation and the like all require the burning of tail gas SO2The ultra-low emission limit is reached, and the prior blast furnace gas purification process can not meet the requirement of SO2And (5) controlling the requirements.
The current technical route mainly comprises source control and tail end treatment after combustion, if a tail end treatment mode is adopted, desulfurization facilities need to be arranged at multiple points, and meanwhile, the waste gas amount after gas combustion is large, and the scale of treatment facilities is enlarged; if a source control mode is adopted, centralized treatment can be realized, and the treated gas amount is only about 60% of the flue gas amount after combustion, so that the total investment is low, the total occupied area is small, the operation cost is low, and the management is convenient. Meanwhile, the source management promotes the service life and the combustion efficiency of the pipe network. The method implements the total sulfur removal of the blast furnace gas, reduces the sulfur content in the gas, can greatly reduce the pressure of the tail end treatment, and even saves tail end treatment facilities.
Blast furnace gas total sulfur removal is a new technical development direction, at present, a single organic sulfur hydrolysis technology and a dry adsorption removal technology are more, and a blast furnace gas dechlorination technology has related application examples, but no reports or engineering cases of the blast furnace gas total sulfur removal technology exist, so the blast furnace gas total sulfur removal technology still belongs to a front-edge exploration stage.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a wet purification device that can realize blast furnace gas complete sulfur desorption, preferably one kind can realize COS, CS in the blast furnace gas2、H2S、SO2And the like, and a wet purification device for removing HCl in a synergistic manner, so as to solve the technical problems.
The utility model relates to a wet purification device capable of realizing total sulfur removal of blast furnace gas, preferably, carbonyl sulfide (COS) and carbon disulfide (CS) in blast furnace gas2) Hydrogen sulfide (H)2S), sulfur dioxide (SO)2) The wet purification device comprises a catalytic hydrolysis tower (2), a desulfurization tower (15), a process water tank (21) and an alkali liquor storage tank (20); the process water tank (21) is connected with the desulfurizing tower (15) and is used for feeding water into the desulfurizing tower (15); the alkali liquor storage tank (20) is connected with the desulfurizing tower (15) and is used for conveying alkali liquor into the desulfurizing tower (15); the catalytic hydrolysis tower (2) is filled with a hydrolysis catalyst and is used for carrying out hydrolysis catalysis on blast furnace gas introduced from the upper part of the catalytic hydrolysis tower (2), the catalytic hydrolysis tower (2) is connected with the lower part of the desulfurizing tower (15) and is used for sending the blast furnace gas after hydrolysis catalysis treatment into the desulfurizing tower (15) for treatment,the top of the desulfurizing tower (15) is provided with a clean blast furnace gas discharge port (27) for discharging the blast furnace gas treated by the desulfurizing tower through the clean blast furnace gas discharge port (27) and sending the blast furnace gas into a blast furnace gas pipe network.
The catalytic hydrolysis tower (2) is provided with a catalytic hydrolysis tower inlet flue, a catalytic hydrolysis tower shell, a catalytic hydrolysis tower outlet flue, a catalyst supporting net (4), a feeding port (3), a discharging port (5) and a sewage discharging port (6), the top end of the catalytic hydrolysis tower shell is connected with the catalytic hydrolysis tower inlet flue and used for feeding blast furnace gas into the catalytic hydrolysis tower (2), the lower end of the catalytic hydrolysis tower shell is connected with the catalytic hydrolysis tower outlet flue, and the catalytic hydrolysis tower outlet flue is connected with the lower part of a desulfurizing tower (15) and used for feeding the blast furnace gas subjected to hydrolysis catalysis treatment into the desulfurizing tower (15) for treatment; the catalyst supporting net (4) is arranged in the shell of the catalytic hydrolysis tower and is used for supporting a hydrolysis catalyst; a sewage outlet (6) is arranged at the bottom end of the catalytic hydrolysis tower shell; the shell of the catalytic hydrolysis tower is provided with a feed inlet (3) and a discharge outlet (5) for feeding and discharging the hydrolysis catalyst.
Wherein, the upper part of the shell of the catalytic hydrolysis tower is conical, the middle part is cylindrical, and the lower part is conical; the catalytic hydrolysis tower inlet flue is arranged at the top end of the upper conical part, the drain outlet (6) is arranged at the bottom end of the lower conical part, and the catalytic hydrolysis tower outlet flue is arranged on the lower conical part and is positioned at the upper part of the drain outlet (6); the catalyst support screen (4) is disposed on the intermediate cylinder.
Wherein the catalyst is one or more of honeycomb, rod, Raschig ring and sphere, and is used for separating carbonyl sulfide (COS) and carbon disulfide (CS) in blast furnace gas2) Catalytic conversion to H by iso-organic sulfur hydrolysis2S, the active component of the catalyst is one or more of Na, K, Fe, Cu and Ni salt, and the carrier is one or more of activated alumina, activated carbon, cordierite and hydrotalcite-like compound.
The catalyst is Raschig annular catalyst, which is randomly stacked on the catalyst support net (4) in the catalytic hydrolysis tower (2) from large to small, and the catalyst is filled with a certain volume, so that the space velocity of the catalytic reaction is 500-4000h-1The flow rate of the flue gas is 0.5-2 m/s; preferably, it is caused to catalyze80-95% of carbonyl sulfide (COS) and carbon disulfide (CS) in volume fraction of blast furnace gas in the hydrolysis tower (2)2) Is catalytically converted into H2S。
Wherein, the height-diameter ratio of the desulfurizing tower is controlled to be 2-5, the gas flow rate is controlled to be 0.5-3m/s, and the uniform air distribution is ensured; preferably, the inlet temperature of blast furnace gas is 40-90 ℃, and the outlet temperature is controlled at 20-40 ℃.
The catalytic hydrolysis tower comprises a catalytic hydrolysis tower, a gas-liquid separation tower, a catalytic hydrolysis tower, a gas-liquid separation tower and a gas-liquid separation tower, wherein an outlet flue of the catalytic hydrolysis tower is connected with an inlet flue of the gas-liquid separation tower, a first layer of circulating water nozzles (11) are installed above the inlet; the type of nozzle is preferably a solid conical nozzle.
The bottom of the desulfurizing tower is preferably conical, a water seal device (10) is arranged at the bottom of the desulfurizing tower and used for receiving reaction waste liquid, a densimeter and a liquid level monitor are arranged in the water seal device (10), an emergency water drain opening (9) and a sewage discharge opening (8) are arranged at the conical bottom end of the desulfurizing tower, a water collecting tank (7) is arranged at the lower part of the desulfurizing tower, a pipeline is led out from the side surface of the water seal device (10) and is connected with a water spraying layer (11) through a circulating water pump (16) and used for enabling part of the waste liquid to directly return to the desulfurizing tower and participate in the chemical reaction process in; the side surface of the water sealing device (10) is also connected with a liquid discharge pump (19) for discharging partial waste liquid; the alkali liquor sprayed on the alkali layer (12) is directly supplied from an alkali liquor storage tank (20) through an alkali liquor pump (17), and the flow of the alkali liquor is increased when the sulfur concentration at the outlet of the desulfurizing tower is too high; the water for washing the water layer (13) is directly supplied from a process water tank (21) through a water supply pump (18); the whole system is filled with water through the water feeding pump (18) at first in the initial stage of equipment operation, the water feeding pump (18) is closed after the system operation is stable, and the water feeding pump (18) is started only when the system needs water supplement or the demisters (13), the alkali liquor nozzles (12) and the circulating water nozzles (11) need to be washed.
Wherein, the main absorbent in the alkali liquor storage tank is sodium hydroxide (NaOH) solution with the mass fraction of 20-32%, preferably, the molar ratio of the sodium hydroxide (NaOH) to the pollutants is controlled to be 1.0-2.0, and the high-efficiency removal of the pollutants in the blast furnace gas is ensured.
The utility model provides a wet purification process capable of realizing total sulfur removal of blast furnace gas, preferably a wet purification process capable of realizing COS and CS in the blast furnace gas2、H2S、SO2A wet purification process for removing sulfur-containing substances and removing HCl in a synergistic manner; which comprises the following steps:
(1) the inlet blast furnace gas (1) firstly enters a catalytic hydrolysis tower (2) for treatment, and COS and CS in the blast furnace gas are treated by a catalyst filled in the catalytic hydrolysis tower (2)2Catalytic conversion to H2S；
(2) Generation of H2S enters a desulfurizing tower (15) along with blast furnace gas, water is sent into the desulfurizing tower (15) by a process water tank (21) through a water feeding pump (18), alkali liquor is sent into the desulfurizing tower (15) by an alkali liquor storage tank (20) through an alkali liquor pump (17), and H is realized under the action of the water and the alkali liquor2S、SO2Simultaneously removing acid gases such as HCl and the like;
(3) the blast furnace gas treated by the desulfurizing tower (15) is discharged through a clean blast furnace gas discharge port (27) and sent into a blast furnace gas pipe network, thereby realizing the desulfurization of the blast furnace gas.
Preferably, the utility model relates to a can realize wet purification device of blast furnace gas total sulfur desorption, preferably one kind can realize carbonyl sulphur (COS), carbon disulfide (CS) among the blast furnace gas2) Hydrogen sulfide (H)2S), sulfur dioxide (SO)2) The wet purification device for removing sulfur-containing substances and removing hydrogen chloride (HCl) in a synergic manner is characterized by comprising a catalytic hydrolysis tower (2), a desulfurization tower (15), a process water tank (21), an alkali liquor storage tank (20), a spray water feeding system, an alkali liquor feeding system and a liquid discharge system. The process water tank (21) and the alkali liquor storage tank (20) are connected with the desulfurizing tower (15) and used for feeding water and alkali liquor into the desulfurizing tower (15), the catalytic hydrolysis tower (2) is filled with hydrolysis catalyst, the catalytic hydrolysis tower (2) is connected with the lower part of the desulfurizing tower (15) and used for feeding blast furnace gas subjected to hydrolysis catalytic treatment into the desulfurizing tower (15) for treatment, the top of the desulfurizing tower (15) is provided with a clean blast furnace gas discharge port (27), and the blast furnace gas subjected to desulfurizing tower treatment is provided with a clean blast furnace gas discharge port (27)The blast furnace gas is discharged through a clean blast furnace gas discharge port (27) and sent into a blast furnace gas pipe network.
Preferably, COS and CS are treated in the catalytic hydrolysis tower (2)2Catalytic conversion to H2S; completion of H in desulfurizing tower2S、SO2Simultaneous removal of HCl, etc.; in order to take safety consideration and convenient maintenance, a bypass is arranged between the blast furnace gas inlet (1) and the blast furnace gas pipe network (27); the whole blast furnace gas equipment and the pipeline system are provided with a dispersion port and a replacement gas interface at the high point, the tail end and the front part of the partition device, and a water seal type drainer at the low point. Catalytic hydrolysis tower (2) have catalytic hydrolysis tower import flue, catalytic hydrolysis tower shell, catalytic hydrolysis tower export flue, catalyst supporting network (4), charge door (3), discharge opening (5) and drain (6), and hydrolysis tower shell top is connected import flue, the lower extreme is connected export flue, catalyst are placed on catalytic hydrolysis tower inside catalyst supporting network (4). The catalytic hydrolysis tower (2) is filled with a catalyst, the catalyst is preferably one or more of honeycomb, rod, Raschig ring and ball, and COS and CS in the blast furnace gas are treated2Catalytic conversion to H by iso-organic sulfur hydrolysis2S, the active component of the catalyst is one or more of Na, K, Fe, Cu and Ni salt, and the carrier is one or more of activated alumina, activated carbon, cordierite and hydrotalcite-like compound. The catalyst configuration is preferably Raschig annular catalyst, the catalyst is randomly stacked on the catalyst support net (4) in the catalytic hydrolysis tower (2) from large to small, and the catalyst is filled with a certain volume, so that the space velocity of the catalytic reaction is 500-4000h-1The flow rate of the flue gas is 0.5-2 m/s; preferably, the volume fraction of COS and CS in the blast furnace gas in the catalytic hydrolysis tower (2) is 80-95 percent2Is catalytically converted into H2And S. The height-diameter ratio of the desulfurizing tower is controlled to be 2-5, the gas flow rate is controlled to be 0.5-3m/s, and the uniform air distribution is ensured; preferably, the inlet temperature of blast furnace gas is 40-90 ℃, and the outlet temperature is controlled at 20-40 ℃.
Install first layer circulating water nozzle (water spray layer) (11) above desulfurizing tower import flue, set up second floor alkali lye nozzle (spout alkali layer) (12) spraying water layer (11) top, set up defroster (13) spraying alkali layer (12) top, set up third layer washing water nozzle (wash water layer) (14) demister (13) top, adopt the mode that the three-layer was spouted in can realize absorbing liquid and coal gas fully to contact, improve material utilization and desulfurization rate. The nozzle type is preferably a solid cone nozzle. The bottom of the desulfurizing tower is provided with a water seal device (10) for receiving reaction waste liquid, a densimeter and a liquid level monitor are arranged in the desulfurizing tower, the bottom end of the desulfurizing tower is provided with an emergency water drain outlet (9) and a sewage discharge outlet (8), the lower part of the desulfurizing tower is provided with a water collecting tank (7), a pipeline is led out from the side surface of the water seal device (10) and is connected with a water spraying layer (11) through a circulating water pump (16), part of the waste liquid directly returns to the desulfurizing tower to participate in the chemical reaction process in the; the alkali liquor sprayed on the alkali layer (12) is directly supplied from an alkali liquor storage tank (20) through an alkali liquor pump (17), and the flow of the alkali liquor is increased when the sulfur concentration at the outlet of the desulfurizing tower is too high; the water for washing the water layer (13) is directly supplied from a process water tank (21) through a water supply pump (18); the whole system is filled with water through the water feeding pump (18) at first in the initial stage of equipment operation, the water feeding pump (18) is closed after the system operation is stable, and the water feeding pump (18) is started only when the system needs water supplement or the demisters (13), the alkali liquor nozzles (12) and the circulating water nozzles (11) need to be washed. The main absorbent in the alkali liquor storage tank is sodium hydroxide (NaOH) solution with the mass fraction of 20-32%, preferably, the molar ratio of the sodium hydroxide (NaOH) to the pollutants is controlled to be 1.0-2.0, and the high-efficiency removal of the pollutants in the blast furnace gas is ensured.
Preferably, the wet purification device comprises a catalytic hydrolysis tower, a desulfurization tower, a process water tank, an alkali liquor storage tank, a spray water feeding system, an alkali liquor feeding system and a liquid discharge system. The process water tank and the alkali liquor storage tank are connected with a desulfurizing tower and used for feeding water and alkali liquor into the desulfurizing tower, a catalytic hydrolysis tower is filled with a hydrolysis catalyst and connected with the lower part of the desulfurizing tower and used for feeding blast furnace gas subjected to hydrolysis catalytic treatment into the desulfurizing tower for treatment, a clean blast furnace gas discharge port is arranged at the top of the desulfurizing tower, and the blast furnace gas treated by the desulfurizing tower is discharged through the clean blast furnace gas discharge port and is fed into a blast furnace gas pipe network. Preferably, wherein COS and CS are reacted in a catalytic hydrolysis column2Catalytic conversion to H2S; completion of H in desulfurizing tower2S、SO2Simultaneous removal of HCl, etc.; for safety consideration and convenient maintenance, a bypass is arranged between the blast furnace gas inlet and the blast furnace gas pipe networkA way; the whole blast furnace gas equipment and the pipeline system are provided with a dispersion port and a replacement gas interface at the high point, the tail end and the front part of the partition device, and a water seal type drainer at the low point.
The principle of the utility model is COS and CS in blast furnace gas2Is catalytically converted into H in a catalytic hydrolysis tower2S; absorbing H in coal gas by water and alkali liquor in desulfurizing tower2S、SO2Acid gases such as HCl; and discharging the treated clean coal gas from the desulfurizing tower and merging the treated clean coal gas into a pipe network. The desulfurization tower adopts a three-layer spraying mode to realize the full contact of the absorption liquid and the flue gas, thereby improving the material utilization rate and the desulfurization rate. The desulfurization waste liquid directly returns to the desulfurizing tower through circulating water pump, improves alkali lye utilization ratio. The spraying water quantity is adjusted according to the water seal liquid level in the operation process and according to the outlet H2The concentration of S is adjusted to spray alkali amount, the liquid discharge amount is adjusted according to the density of the desulfurization waste liquid, the removal of sulfur-containing substances in blast furnace gas is realized, and SO is solved from the source2The problem of exceeding standard is solved, and meanwhile, the corrosion problem of the gas pipeline is controlled to a certain extent by the synergistic removal of HCl.
The utility model provides a technical process is simple, the cost is low, the reliability is good, especially can be in 40-90 ℃ temperature interval, realize H among the blast furnace gas2S、SO2And wet purification process for removing HCl and other acidic gases.
The utility model has the advantages that: the utility model provides a realize H in blast furnace gas simultaneously2S、SO2And wet purification process for removing HCl and other acidic gases. The purification process of the utility model firstly uses COS and CS2Isoorganosulfur catalytic conversion to H2And S, then, removing the acid gas by spraying water and alkali liquor. The process can provide accurate process layout scheme and operation parameters for controlling the sulfur pollutants in the blast furnace gas for steel mills and environmental protection companies, and solve the problem of SO from the source2The problem of exceeding standard is solved, meanwhile, the problem of corrosion of the gas pipeline is controlled to a certain extent by the synergistic removal of HCl, the process is simple, the reliability is good, the operation is stable, and the pollutant control cost is reduced.
Drawings
FIG. 1 is a process flow diagram of a wet scrubbing unit for the desulfurization of blast furnace gas;
fig. 2 is a layout diagram of a wet scrubbing unit for the desulfurization of blast furnace gas.
The labels in the figure are: 1-inlet blast furnace gas, 2-catalytic hydrolysis tower, 3-catalytic hydrolysis tower feed inlet, 4-catalyst supporting net, 5-catalytic hydrolysis tower discharge outlet, 6-catalytic hydrolysis tower discharge outlet, 7-water collecting tank, 8-desulfurization tower discharge outlet, 9-desulfurization tower emergency water discharge outlet, 10-desulfurization tower water seal device, 11-first layer process water nozzle (water spray layer), 12-second layer alkali liquor nozzle (alkali spray layer), 13-demister, 14-third layer flushing water nozzle (water flushing layer), 15-desulfurization tower, 16-circulating water pump, 17-alkali liquor pump, 18-water feeding pump, 19-liquid discharge pump, 20-alkali liquor storage tank, 21-process water tank, 22-flushing water valve, 23-flushing water to alkali liquor pipeline bypass valve, 24-an alkali liquor pipeline stop valve, 25-a by-pass valve of flushing water to a circulating water pipeline, 26-a circulating water pipeline stop valve and 27-outlet blast furnace gas.
Detailed Description
As shown in figures 1 and 2, a wet purification device capable of realizing total sulfur removal of blast furnace gas, preferably a wet purification device capable of realizing COS and CS in the blast furnace gas2、H2S、SO2The wet purification device for removing sulfur-containing substances and removing HCl in a synergistic manner comprises a catalytic hydrolysis tower 2, a desulfurization tower 15, a process water tank 21, an alkali liquor storage tank 20, a spray water feeding system, an alkali liquor feeding system and a liquid discharging system. The process water tank 21 and the alkali liquor storage tank 20 are connected with the desulfurizing tower 15 and used for feeding water and alkali liquor into the desulfurizing tower 15, the catalytic hydrolysis tower 2 is filled with hydrolysis catalyst, the catalytic hydrolysis tower 2 is connected with the lower part of the desulfurizing tower 15 and used for feeding blast furnace gas subjected to hydrolysis catalytic treatment into the desulfurizing tower 15 for treatment, the top of the desulfurizing tower 15 is provided with a clean blast furnace gas discharge port 27, and the blast furnace gas subjected to desulfurizing tower treatment is discharged through the clean blast furnace gas discharge port 27 and is fed into a blast furnace gas pipe network.
As shown in fig. 2, the catalytic hydrolysis tower 2 is provided with a catalytic hydrolysis tower inlet flue, a catalytic hydrolysis tower shell, a catalytic hydrolysis tower outlet flue, a catalyst supporting net 4, a charging opening 3, a discharging opening 5 and a sewage discharging opening 6, the top end of the hydrolysis tower shell is connected with the inlet flue, and the lower end is connected with the outlet flueThe catalyst is placed on a catalyst support screen 4 inside the catalytic hydrolysis tower. The catalytic hydrolysis tower 2 is filled with a catalyst, the catalyst is preferably one or more of honeycomb, rod, Raschig ring and ball, and COS and CS in the blast furnace gas are treated2Catalytic conversion to H by iso-organic sulfur hydrolysis2S, the active component of the catalyst is one or more of Na, K, Fe, Cu and Ni salt, and the carrier is one or more of activated alumina, activated carbon, cordierite and hydrotalcite-like compound. The catalyst configuration is preferably Raschig annular catalyst, the catalyst is randomly stacked on the catalyst support net 4 in the catalytic hydrolysis tower 2 from large to small, and the catalyst is filled in a certain volume, so that the space velocity of the catalytic reaction is 500-4000h-1The flow rate of the flue gas is 0.5-2 m/s; preferably, the volume fraction of COS and CS in the blast furnace gas in the catalytic hydrolysis tower 2 is 80-95 percent2Is catalytically converted into H2S。
As shown in FIGS. 1 and 2, COS and CS are introduced into a catalytic hydrolysis column 22Catalytic conversion to H2S; completion of H in desulfurizing tower2S、SO2And HCl, etc. The height-diameter ratio of the desulfurizing tower is controlled to be 2-5, the gas flow rate is controlled to be 0.5-3m/s, and the uniform air distribution is ensured; preferably, the inlet temperature of blast furnace gas is 40-90 ℃, and the outlet temperature is controlled at 20-40 ℃. Install first layer circulating water nozzle (spout the water layer) 11 above desulfurizing tower import flue, set up second floor alkali lye nozzle (spout the alkali layer) 12 above spraying water layer 11, set up defroster 13 above spouting alkali layer 12, set up third layer washing water nozzle (wash the water layer) 14 above defroster 13, adopt the mode that the three-layer was spouted and can realize that absorption liquid and coal gas fully contact, improve material utilization and desulfurization rate. The nozzle type is preferably a solid cone nozzle.
As shown in fig. 2, a water seal device 10 is arranged at the bottom of the desulfurization tower and used for receiving reaction waste liquid, a densimeter and a liquid level monitor are arranged in the water seal device, an emergency water drain 9 and a sewage drain 8 are arranged at the bottom end of the water seal device, a water collecting tank 7 is arranged at the lower part of the water seal device 10, a pipeline is led out from the side surface of the water seal device 10 and is connected with a water spraying layer 11 through a circulating water pump 16, part of the waste liquid directly returns to the desulfurization tower and participates in; the alkali liquor of the alkali spraying layer 12 is directly supplied by an alkali liquor storage tank 20 through an alkali liquor pump 17, and the flow of the alkali liquor is increased when the sulfur concentration at the outlet of the desulfurizing tower is too high; wherein, the main absorbent in the alkali liquor storage tank is NaOH solution with the mass fraction of 20-32%, preferably, the molar ratio of NaOH to pollutants is controlled at 1.0-2.0, and the high-efficiency removal of the pollutants in the blast furnace gas is ensured.
As shown in fig. 2, a flushing water valve 22 is arranged between the flushing water nozzle 14 and the water feed pump 18, a lye pipeline cut-off valve 24 is arranged between the lye nozzle 12 and the lye pump 17, and a circulating water pipeline cut-off valve 26 is arranged between the circulating water nozzle 11 and the circulating water pump 16; meanwhile, in order to meet the requirement of flushing the alkali liquor nozzle and the circulating water nozzle in the operation process, a bypass is led out from a pipeline between the flushing water valve 22 and the water feeding pump 18 and is respectively connected to an alkali liquor pipeline stop valve 24 and a circulating water pipeline stop valve 26, and a flushing water-to-alkali liquor pipeline bypass valve 23 and a flushing water-to-circulating water pipeline bypass valve 25 are installed on two bypass pipelines. The water for washing the water layer 14 is supplied directly from the process water tank 21 through the feed pump 18; in the initial stage of equipment operation, firstly, the flushing water valve 22 and the alkali liquor pipeline stop valve 24 are opened, the whole system is filled with water and main absorbent through the water feed pump 18 and the alkali liquor pump 17, the water feed pump 18 and the flushing water valve 22 are closed after the system is stably operated, the circulating water pipeline stop valve 26 is opened, and part of waste liquid directly returns to the desulfurizing tower to participate in the reaction process again. When the device is in normal operation, the alkali liquor pipeline stop valve 24 and the circulating water pipeline stop valve 26 are normally opened, and the flushing water valve 22, the flushing water-to-alkali liquor pipeline bypass valve 23 and the flushing water-to-circulating water pipeline bypass valve 25 are normally closed. When the system needs to be supplemented with water or the demister 13 needs to be cleaned, the flushing water valve 22 is opened; when the alkali liquor nozzle needs to be washed, the alkali liquor pipeline cut-off valve 24 is closed, and the washing water is opened to the alkali liquor pipeline bypass valve 23; when the circulating water nozzle needs to be flushed, the circulating water pipeline cut-off valve 26 is closed, and the flushing water is opened to the circulating water pipeline bypass valve 25.
As shown in figures 1 and 2, a wet purification process capable of realizing total sulfur removal of blast furnace gas, preferably a wet purification process capable of realizing COS and CS in the blast furnace gas2、H2S、SO2The wet purification process for removing the sulfur-containing substances and removing HCl in a synergistic manner preferably adopts one of the processes shown in figures 1 and 2 which can realize the total sulfur of the blast furnace gasA wet purification process of removal; the method is characterized by comprising the following steps:
(1) the inlet blast furnace gas 1 firstly enters a catalytic hydrolysis tower 2 for treatment, and COS and CS in the blast furnace gas are treated by a catalyst filled in the catalytic hydrolysis tower 22Catalytic conversion to H2S；
(2) Generation of H2S enters the desulfurizing tower 15 along with blast furnace gas, water is sent into the desulfurizing tower 15 by the process water tank 21 through the water feeding pump 18, alkali liquor is sent into the desulfurizing tower 15 by the alkali liquor storage tank 20 through the alkali liquor pump 17, and H is realized under the action of the water and the alkali liquor2S、SO2Simultaneously removing acid gases such as HCl and the like;
(3) the blast furnace gas treated by the desulfurizing tower 15 is discharged through the clean blast furnace gas discharge port 27 and sent into a blast furnace gas pipe network, thereby realizing the total sulfur removal of the blast furnace gas.
The spraying water quantity is adjusted according to the water seal liquid level in the operation process and according to the outlet H2The concentration of S is adjusted to spray alkali amount, the liquid discharge amount is adjusted according to the density of the desulfurization waste liquid, the removal of sulfur-containing substances in blast furnace gas is realized, and SO is solved from the source2The problem of exceeding standard is solved, and meanwhile, the corrosion problem of the gas pipeline is controlled to a certain extent by the synergistic removal of HCl.
The technical process of the utility model is as follows: combustible gas (containing nitrogen (N)) as byproduct in blast furnace iron-making production process2) Carbon monoxide (CO) and carbon dioxide (CO)2) Hydrogen (H)2) Hydrocarbons, a small amount of sulfur-containing compounds and dust) through gravity dust removal, bag dust removal, and a residual pressure turbine power generation unit (TRT), just as the inlet blast furnace gas 1 of the purification process. The blast furnace gas passes through the catalytic hydrolysis tower 2, and the catalytic hydrolysis tower 2 is filled with a catalyst. The catalyst takes one or more of active alumina, active carbon, cordierite and hydrotalcite-like compound as a carrier, one or more of Na, K, Fe, Cu and Ni salts as an active component, and the configuration of the catalyst is a Raschig annular catalyst. The catalyst is filled in a certain volume, so that the space velocity of the catalytic reaction is 500-4000h-1The gas flow rate is 0.5-2m/s, so that 80-95% of COS and CS in the blast furnace gas in the catalytic hydrolysis tower 2 are in volume fraction2Is catalytically converted into H2And S. And then enters the desulfurization tower of fig. 2. Water and alkali liquor pass through a water feed pump 18 and an alkali liquor pump 17, are sent into the desulfurizing tower from a process water tank 21 and an alkali liquor storage tank 20 through a third layer flushing water nozzle (flushing water layer) 14 and a second layer alkali liquor nozzle (alkali liquor spraying layer) 12 in the picture 2, a pipeline is led out from the side surface of a water seal device 10 at the bottom of the desulfurizing tower, and is connected with a first layer process water nozzle (water spraying layer) 11 through a circulating water pump 16, and partial waste liquid directly returns to the desulfurizing tower to participate in the chemical reaction process in the desulfurizing tower again.
In the catalytic hydrolysis tower, the blast furnace gas and the moisture react under the action of a catalyst as follows:
COS+H20＝CO2+H2S；
CS2+H20＝COS+H2S；
CS2+2H2O＝2H2S+CO2。
h produced by subsequent reaction2S and small amount of HCl and SO in blast furnace gas2And (3) waiting the acid gas to react with the absorbent as follows:
HCl+NaOH＝NaCl+H2O；
when NaOH is small, H2S+NaOH＝NaHS+H2O，SO2+NaOH＝NaHSO3；
When NaOH is excessive, H2S+2NaOH＝Na2S+2H2O，SO2+2NaOH＝Na2SO3+H2O；
O2When present, NaHSO3And Na2SO3Can be oxidized to Na2SO4。
Example (b):
the blast furnace gas of a certain steel mill adopts the device and the process of the utility model, the temperature of the inlet gas of the catalytic hydrolysis tower is 90 ℃, COS and CS2The content is 120mg/Nm3，H2S content of 50mg/Nm3The inlet gas flow rate is 5000Nm3H, 2.5m is filled in the catalytic hydrolysis tower3The cross-sectional area of the catalyst perpendicular to the flow direction of the flue gas is 1.5m2The flow velocity of flue gas in the catalytic hydrolysis tower is 1m/s, and the flue gas passes through the catalytic hydrolysis tower, COS and CS2Catalytic conversion to H2The proportion of S was 91%. Blast furnace gas enters the desulfurizing tower through a lateral inlet at the lower part of the desulfurizing tower, the diameter of the section of the desulfurizing tower is 1.4m, and the apparent flow velocity of flue gas is 1.2 m/s. The first water spraying layer has 7 nozzles in total, and the spraying capacity of each nozzle is 500L/m3(ii) a The second alkali spraying layer is provided with 4 nozzles in total, and the spraying capacity of each nozzle is 100L/m3(ii) a The third layer of rinsing water layer had 7 nozzles in total, and the single nozzle had a spraying capacity of 500L/m3. The NaOH content in the alkali liquor is 32 percent, the mol ratio of NaOH to pollutants is controlled to be 1.0-2.0, and the temperature of outlet coal gas is 40 ℃. After the wet purification process, COS and CS2Conversion efficiency is greater than 90%, and outlet H2The S concentration is less than 15 mg/Nm.
The above embodiments are not limited to the above embodiments, but also other combinations of related devices are also the scope of the present invention, and the above embodiments are only for illustrative purposes, rather than for the limitations of the present invention, and those skilled in the relevant art can make various changes and modifications without departing from the spirit and scope of the present invention, and therefore all equivalent technical solutions should also belong to the scope of the present invention.

Claims (9)

1. A wet purification device for total sulfur removal of blast furnace gas is characterized by comprising a catalytic hydrolysis tower (2), a desulfurization tower (15), a process water tank (21) and an alkali liquor storage tank (20); the process water tank (21) is connected with the desulfurizing tower (15) and is used for feeding water into the desulfurizing tower (15); the alkali liquor storage tank (20) is connected with the desulfurizing tower (15) and is used for conveying alkali liquor into the desulfurizing tower (15); the catalytic hydrolysis tower (2) is filled with a hydrolysis catalyst and is used for carrying out hydrolysis catalysis on blast furnace gas introduced from the upper part of the catalytic hydrolysis tower (2), the catalytic hydrolysis tower (2) is connected with the lower part of the desulfurizing tower (15) and is used for sending the blast furnace gas subjected to hydrolysis catalysis treatment into the desulfurizing tower (15) for treatment, and the top of the desulfurizing tower (15) is provided with a clean blast furnace gas discharge port (27) and is used for discharging the blast furnace gas subjected to the desulfurization treatment through the clean blast furnace gas discharge port (27) and sending the blast furnace gas into a blast furnace gas pipe network.
2. The wet purification device according to claim 1, wherein the catalytic hydrolysis tower (2) is provided with a catalytic hydrolysis tower inlet flue, a catalytic hydrolysis tower shell, a catalytic hydrolysis tower outlet flue, a catalyst support net (4), a feed inlet (3), a discharge opening (5) and a catalytic hydrolysis tower drain outlet (6), the top end of the catalytic hydrolysis tower shell is connected with the catalytic hydrolysis tower inlet flue and used for feeding blast furnace gas into the catalytic hydrolysis tower (2), the lower end of the catalytic hydrolysis tower shell is connected with the catalytic hydrolysis tower outlet flue, and the catalytic hydrolysis tower outlet flue is connected with the lower part of the desulfurization tower (15) and used for feeding the blast furnace gas after hydrolysis catalytic treatment into the desulfurization tower (15) for treatment; the catalyst supporting net (4) is arranged in the shell of the catalytic hydrolysis tower and is used for supporting a hydrolysis catalyst; the bottom end of the shell of the catalytic hydrolysis tower is provided with a sewage draining outlet (6) of the catalytic hydrolysis tower; the shell of the catalytic hydrolysis tower is provided with a feed inlet (3) and a discharge outlet (5) for feeding and discharging the hydrolysis catalyst.
3. The wet purification apparatus of claim 2, wherein the catalytic hydrolysis tower has a conical upper housing part, a cylindrical middle housing part, and a conical lower housing part; the inlet flue of the catalytic hydrolysis tower is arranged at the top end of the upper conical part, the drain outlet (6) of the catalytic hydrolysis tower is arranged at the bottom end of the lower conical part, and the outlet flue of the catalytic hydrolysis tower is arranged on the lower conical part and is positioned at the upper part of the drain outlet (6) of the catalytic hydrolysis tower; the catalyst support screen (4) is disposed on the intermediate cylinder.
4. The wet scrubbing apparatus of any one of claims 1 to 3, wherein said catalyst is one or more of honeycomb, rod, raschig ring, and sphere for converting carbonyl sulfide (COS) and carbon disulfide (CS) in blast furnace gas2) Catalytic conversion to H by iso-organic sulfur hydrolysis2S, the active component of the catalyst is one or more of Na, K, Fe, Cu and Ni salt, and the carrier is one or more of activated alumina, activated carbon, cordierite and hydrotalcite-like compound.
5. The wet purification device according to claim 4, wherein the catalyst is a Raschig ring catalyst, and is randomly stacked from large to small on the catalyst support net (4) in the catalytic hydrolysis tower (2).
6. The wet scrubbing apparatus of any one of claims 1 to 3, wherein the aspect ratio of the desulfurization tower is controlled to be 2 to 5.
7. The wet purification apparatus as claimed in any one of claims 1 to 3, wherein the catalytic hydrolysis tower outlet flue is connected to the desulfurization tower inlet flue, a first layer of circulating water nozzles (11) is installed above the desulfurization tower inlet flue to form a water spray layer, a second layer of lye nozzles (12) is installed above the water spray layer to form a alkali spray layer, a demister (13) is installed above the alkali spray layer, and a third layer of rinsing water nozzles (14) is installed above the demister (13) to form a rinsing water layer.
8. The wet purification device according to claim 7, wherein the bottom of the desulfurization tower is provided with a water seal device (10) for receiving the reaction waste liquid, a densimeter and a liquid level monitor are arranged in the water seal device (10), the conical bottom end of the desulfurization tower is provided with an emergency water outlet (9) and a desulfurization tower sewage outlet (8), the lower part of the desulfurization tower is provided with a water collecting tank (7), a pipeline is led out from the side surface of the water seal device (10) and is connected with a water spraying layer through a circulating water pump (16) for directly returning part of the waste liquid to the desulfurization tower; the side surface of the water seal device (10) is also connected with a liquid discharge pump (19) for discharging partial waste liquid.
9. The wet scrubbing apparatus of any one of claims 1 to 3, wherein the primary absorbent in the lye storage tank is a sodium hydroxide (NaOH) solution having a mass fraction of 20% to 32%.
CN202021580345.6U 2020-08-03 2020-08-03 Wet purification device for total sulfur removal of blast furnace gas Active CN212713388U (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115400533A (en) * 2022-08-23 2022-11-29 天津绿菱气体有限公司 Method and device for recycling carbonyl sulfide tail gas

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115400533A (en) * 2022-08-23 2022-11-29 天津绿菱气体有限公司 Method and device for recycling carbonyl sulfide tail gas
CN115400533B (en) * 2022-08-23 2023-06-30 天津绿菱气体有限公司 Method and device for recycling carbonyl sulfide tail gas

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