CN210528472U - Sulfuric acid regeneration system - Google Patents
Sulfuric acid regeneration system Download PDFInfo
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- CN210528472U CN210528472U CN201921557247.8U CN201921557247U CN210528472U CN 210528472 U CN210528472 U CN 210528472U CN 201921557247 U CN201921557247 U CN 201921557247U CN 210528472 U CN210528472 U CN 210528472U
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- gas
- tower
- pipe
- absorption tower
- sulfuric acid
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- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 title claims abstract description 73
- 230000008929 regeneration Effects 0.000 title claims abstract description 14
- 238000011069 regeneration method Methods 0.000 title claims abstract description 14
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 claims abstract description 44
- 239000007788 liquid Substances 0.000 claims abstract description 44
- 238000012856 packing Methods 0.000 claims abstract description 43
- 238000006243 chemical reaction Methods 0.000 claims abstract description 27
- 238000009826 distribution Methods 0.000 claims abstract description 24
- 239000012535 impurity Substances 0.000 claims abstract description 12
- 238000001556 precipitation Methods 0.000 claims abstract description 9
- 238000000746 purification Methods 0.000 claims abstract description 8
- 239000007921 spray Substances 0.000 claims abstract description 8
- 238000010521 absorption reaction Methods 0.000 claims description 69
- 239000002253 acid Substances 0.000 claims description 51
- AKEJUJNQAAGONA-UHFFFAOYSA-N sulfur trioxide Chemical compound O=S(=O)=O AKEJUJNQAAGONA-UHFFFAOYSA-N 0.000 claims description 46
- 241000736911 Turritella communis Species 0.000 claims description 35
- 239000003054 catalyst Substances 0.000 claims description 31
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 21
- 239000000919 ceramic Substances 0.000 claims description 14
- 238000009825 accumulation Methods 0.000 claims description 13
- 238000011068 loading method Methods 0.000 claims description 13
- 238000005507 spraying Methods 0.000 claims description 12
- 238000003860 storage Methods 0.000 claims description 12
- 238000010438 heat treatment Methods 0.000 claims description 9
- 238000005086 pumping Methods 0.000 claims description 9
- 238000009434 installation Methods 0.000 claims description 6
- 238000001802 infusion Methods 0.000 claims description 4
- 238000004062 sedimentation Methods 0.000 claims description 4
- 230000005540 biological transmission Effects 0.000 claims description 3
- 229910010293 ceramic material Inorganic materials 0.000 claims description 3
- 230000008878 coupling Effects 0.000 claims 1
- 238000010168 coupling process Methods 0.000 claims 1
- 238000005859 coupling reaction Methods 0.000 claims 1
- 239000010865 sewage Substances 0.000 claims 1
- 239000000945 filler Substances 0.000 abstract description 12
- 238000000034 method Methods 0.000 abstract description 4
- 230000003197 catalytic effect Effects 0.000 abstract description 2
- 230000035484 reaction time Effects 0.000 abstract description 2
- 235000011149 sulphuric acid Nutrition 0.000 abstract description 2
- 239000001117 sulphuric acid Substances 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 92
- 239000000839 emulsion Substances 0.000 description 7
- 239000004810 polytetrafluoroethylene Substances 0.000 description 7
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 7
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 238000001035 drying Methods 0.000 description 4
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 3
- 229910001882 dioxygen Inorganic materials 0.000 description 3
- 238000011049 filling Methods 0.000 description 3
- 239000006260 foam Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000003595 mist Substances 0.000 description 3
- 230000003247 decreasing effect Effects 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000005096 rolling process Methods 0.000 description 2
- 238000010306 acid treatment Methods 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000002407 reforming Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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Abstract
The utility model provides a sulphuric acid regeneration system, is including the sulfur dioxide purification packed tower, desicator, conversion tower and the sour equipment of system that connect gradually, sulfur dioxide purification packed tower includes tower casing, filler bearing plate, spray set, first admission line, packing layer and impurity precipitation device, and the top of tower casing is provided with the outlet duct, and the bottom of tower casing is provided with the drain pipe, and the filler bearing plate includes gas distribution board and a set of gas-lift tube, is provided with a set of ponding groove on the gas distribution board. The utility model has the advantages that: the filler bearing plate simultaneously plays the roles of supporting the filler and uniformly distributing the air flow, so that the space in the filler tower is saved, and the liquid and the gas in the tower are more fully reacted. The reaction efficiency is improved by changing the structure of the existing catalytic region; the steam in the conveying process is utilized, and the reaction time in the reactor is shortened.
Description
Technical Field
The utility model relates to a spent acid treatment facility field, concretely relates to sulphuric acid regeneration system.
Background
At present, acid gas generated by cracking waste sulfuric acid contains sulfur dioxide and sulfur trioxide, and after the acid gas enters a packed tower, the acid gas is contacted with water flowing down above the packed tower, and the water absorbs the sulfur trioxide in the acid gas to form an acid solution which falls to the bottom of the tower and is discharged through a liquid outlet; the sulfur dioxide gas is discharged through a gas outlet at the top of the tower. The acid gas filtered by the existing packed tower has high humidity, and the problems of non-uniform contact between liquid and gas and insufficient gas reaction and filtration exist. The sulfuric acid production line needs to mix sulfur dioxide and oxygen to produce sulfur trioxide, the reaction between the sulfur dioxide and the oxygen is carried out through a reactor, the existing reactor 1 has poor using effect and low reaction efficiency, and a catalyst blocks a microporous plate in the reaction process to generate high pressure; 2. because high temperature is needed in the reaction process, the steam is directly driven into the existing steam heating pipeline, and the energy in the process of transportation is wasted. The sulfur trioxide absorption tower of the existing acid making device often has the defect of low absorption efficiency, so that the absorbed tail gas contains more sulfur trioxide gas.
SUMMERY OF THE UTILITY MODEL
The utility model aims to provide a sulfuric acid regeneration system aiming at the defects.
The utility model comprises a sulfur dioxide purifying packed tower, a dryer, a conversion tower and an acid making device which are connected in sequence,
the sulfur dioxide purification packed tower comprises a tower shell, a packing supporting plate, a spraying device, a first air inlet pipeline, a packing layer and an impurity precipitation device, wherein an air outlet pipe is arranged at the top of the tower shell, a liquid outlet pipe is arranged at the bottom of the tower shell, the packing supporting plate comprises a gas distribution plate and a group of riser pipes, a group of liquid accumulation tanks are arranged on the gas distribution plate, a group of liquid through holes are formed in the bottom of each liquid accumulation tank, a group of cylindrical riser pipe mounting seats are arranged between every two adjacent liquid accumulation tanks, a group of vent holes are annularly and uniformly distributed on the upper pipe wall of each riser pipe, a liquid baffle plate is arranged at the top of each riser pipe, the group of riser pipes are mounted on the corresponding cylindrical riser pipe mounting seats, the packing supporting plate is mounted in the tower shell, the spraying device comprises a water inlet main pipe and a group of branch pipes, one end of the water inlet main, the device comprises a water inlet main pipe, a group of branch pipes, a spraying device, a packing support plate, a packing layer, an impurity precipitation device and a sedimentation tank, wherein the water inlet main pipe is provided with a group of nozzles, the end parts of the group of branch pipes are respectively provided with a nozzle, a packing installation area is formed between the spraying device and the packing support plate, the packing layer is installed in the packing installation area, the air outlet end of a first air inlet pipe is positioned in a tower shell and below the packing support plate, the air inlet end of the first air inlet pipe is positioned outside the tower shell, the impurity precipitation device comprises a U-shaped pipe and a sedimentation tank, the inlet end of the U-shaped pipe is communicated;
the air outlet pipe at the top of the tower shell is connected with the air inlet of the dryer;
the conversion tower comprises a reaction box body and a group of catalyst placing boxes, a steam heating sleeve and a gas outlet are arranged on the reaction box body, a pair of steam inlets and a steam outlet are arranged on the steam heating sleeve, a first steam pipeline and a second steam pipeline which are respectively communicated with the pair of steam inlets are arranged on the pair of steam inlets, the catalyst placing boxes comprise a silk screen, a ceramic carrier adhered with the catalyst and a loading box, a plurality of groups of air holes are formed in the bottom of the loading box, the ceramic carrier adhered with the catalyst is positioned in the loading box, the silk screen is detachably arranged on the top of the loading box, a gas distributor and a group of catalyst placing boxes are arranged at the top in the reaction box body, the gas distributor and the group of catalyst placing boxes are sequentially arranged from top to bottom, and a gas outlet of the gas distributor is positioned above the silk screen of the uppermost layer of the group, one end of the first gas pipeline and one end of the second gas pipeline respectively penetrate through the first steam pipeline and the second steam pipeline and are communicated with a gas inlet of the gas distributor, and the first gas pipeline is connected with a gas outlet of the dryer;
the acid making equipment comprises a first absorption tower, a second absorption tower and a sulfuric acid storage tank; concentrated sulfuric acid inlets and sulfuric acid liquid discharge ports are formed in the lower portions of the first absorption tower and the second absorption tower, filling portions are formed in the first absorption tower and the second absorption tower, an acid distributor is arranged above the filling portions, and a sulfur trioxide distribution mechanism is arranged below the filling portions; the sulfur trioxide distribution mechanism comprises a first cylinder fixedly connected with the inner wall of a first absorption tower, a second cylinder sleeved in the first cylinder, an upper annular plate and a lower annular plate which seal the upper and lower ends of the first cylinder and the second cylinder, and a plurality of exhaust pipes vertically arranged on the lower annular plate, wherein a cavity is formed among the first cylinder, the second cylinder, the upper annular plate and the lower annular plate; the upper parts of the first absorption tower and the second absorption tower are respectively provided with a demister, the top of the first absorption tower is provided with a gas transmission pipeline which is communicated with a cavity part at the lower part of the second absorption tower, the top of the second absorption tower is provided with a tail gas discharge pipe, the lower parts of the first absorption tower and the second absorption tower are respectively connected with an acid pumping pipeline, an acid liquor conveying pump and a heat exchanger are arranged on the acid pumping pipeline, and the outlet end of the acid pumping pipeline is connected to the acid distributor; the sulfuric acid liquid outlet is connected with an acid discharge pipeline communicated with the top of the sulfuric acid storage tank.
It also has the defoaming silk screen, and the center of defoaming silk screen is upwards protruding, forms the hemisphere face, and the defoaming silk screen is installed in the tower shell to be located spray set top.
The air outlet of the first air inlet pipeline faces to the center of the bottom of the tower shell.
And the air outlet pipe, the liquid outlet pipe, the water inlet main pipe and the first air inlet pipeline are respectively provided with a shutoff valve.
The lengths of the liquid accumulating tanks are sequentially decreased from the center to the outer diameter of the gas distribution plate.
The outer wall of the cylindrical riser mounting seat is provided with external threads, and the inner wall of the bottom of the riser is provided with internal threads matched with the external threads.
The first cylinder, the second cylinder, the upper annular plate, the lower annular plate and the exhaust pipe are all made of ceramic materials.
The diameter of the second cylinder is three fifths of the diameter of the first absorption tower and the second absorption tower.
The sulfuric acid storage tank is communicated with the lower parts of the first absorption tower and the second absorption tower through a pipeline and an infusion pump.
The utility model has the advantages that: the filler bearing plate simultaneously plays the roles of supporting the filler and uniformly distributing the air flow, so that the space in the filler tower is saved, and the liquid and the gas in the tower are more fully reacted. The reaction efficiency is improved by changing the structure of the existing catalytic region; the steam in the conveying process is utilized, and the reaction time in the reactor is shortened.
Drawings
Fig. 1 is a schematic view of the connection structure of the present invention.
FIG. 2 is a schematic diagram of a sulfur dioxide purification packed tower.
FIG. 3 is a schematic sectional view of a sulfur dioxide purifying packed tower.
Fig. 4 is a schematic view of the top surface of the packing support plate.
Fig. 5 is a schematic view of the structure of the bottom surface of the packing support plate.
Fig. 6 is a schematic structural view of the shower apparatus.
FIG. 7 is a schematic view of a reforming tower structure.
Fig. 8 is a partially enlarged schematic view of fig. 7 a.
Fig. 9 is a partially enlarged schematic view of fig. 7 b.
Fig. 10 is a schematic view of the structure of the catalyst placing case.
Fig. 11 is a structural diagram of the mounting position of the upper triangular guide plate.
Fig. 12 is a schematic structural view of an acid producing apparatus.
FIG. 13 is a schematic view of the sulfur trioxide distribution mechanism.
Fig. 14 is a schematic view of the structure of the lower annular plate.
Fig. 15 is a schematic view of the structure of the exhaust pipe.
Detailed Description
As shown in the attached drawing, the utility model comprises a sulfur dioxide purification packed tower 500, a dryer 501, a conversion tower 502 and an acid making device 503 which are connected in sequence,
the sulfur dioxide purification packed tower 500 comprises a tower shell 201, a packing support plate 202, a spraying device 203, a first air inlet pipeline 204, a packing layer 205 and an impurity precipitation device, wherein an air outlet pipe 206 is arranged at the top of the tower shell 201, an liquid outlet pipe 218 is arranged at the bottom of the tower shell 201, the packing support plate 202 comprises an air distribution plate 207 and a group of riser pipes 208, a group of liquid accumulation tanks 209 are arranged on the air distribution plate 207, a group of liquid through holes 211 are formed at the bottom in each liquid accumulation tank 209, a group of cylindrical riser pipe mounting seats 210 are arranged between every two adjacent liquid accumulation tanks 209, a group of vent holes 212 are uniformly distributed on the upper pipe wall of each riser pipe 208 in an annular manner, a liquid baffle plate 1213 is arranged at the top of each riser pipe 208, a group of riser pipes 208 are mounted on the corresponding cylindrical riser pipe mounting seats 210, the packing support plate 202 is mounted in the tower shell 201, one end of a water inlet header pipe 213 is positioned in the tower shell 201, the other end of the water inlet header pipe is positioned outside the tower shell 201, a group of branch pipes 214 are communicated with the water inlet header pipe 213, a group of spray heads 215 are arranged on the water inlet header pipe 213, the end parts of the group of branch pipes 214 are respectively provided with the spray heads 215, a packing installation area is formed between the spray device 203 and the packing support plate 202, a packing layer 205 is installed in the packing installation area, the air outlet end of a first air inlet pipe 204 is positioned in the tower shell 201 and below the packing support plate 202, the air inlet end of the first air inlet pipe 204 is positioned outside the tower shell 201, the impurity precipitation device comprises a U-shaped pipe 216 and a precipitation tank 217, the inlet end of the U-shaped pipe 216 is communicated with the outlet end of a liquid outlet pipe 218, the bottom of the U-shaped pipe 216;
the air outlet pipe 206 at the top of the tower shell 201 is connected with the air inlet of the dryer 501;
the conversion tower 502 comprises a reaction box body 1 and a group of catalyst placing boxes 2, a steam heating jacket 3 and a gas outlet are arranged on the reaction box body 1, a pair of steam inlets and a steam outlet are arranged on the steam heating jacket 3, a first steam pipeline and a second steam pipeline which are respectively communicated with the pair of steam inlets are arranged on the pair of steam inlets, the catalyst placing boxes 2 comprise a silk screen 6, a ceramic carrier 7 adhered with a catalyst and a loading box 8, a plurality of groups of air holes are formed in the bottom of the loading box 8, the ceramic carrier 7 adhered with the catalyst is positioned in the loading box 8, the silk screen 6 is detachably arranged on the top of the loading box 8, a gas distributor 9 and a group of catalyst placing boxes 2 are arranged at the top in the reaction box body 1, the gas distributor 9 and the group of catalyst placing boxes 2 are sequentially arranged from top to bottom, and a gas outlet of the gas distributor 9 is positioned above the silk screen 6 of the uppermost layer of the group of catalyst placing, one end of a first gas pipeline 4 and one end of a second gas pipeline 5 respectively penetrate through the first steam pipeline and the second steam pipeline and are communicated with a gas inlet of a gas distributor 9, and the first gas pipeline 4 is connected with a gas outlet of the dryer 501;
the acid making equipment comprises a first absorption tower 61, a second absorption tower 62 and a sulfuric acid storage tank 63; concentrated sulfuric acid inlets 64 and sulfuric acid liquid outlets 65 are formed in the lower portions of the first absorption tower 61 and the second absorption tower 62, filler portions 66 are formed in the first absorption tower 61 and the second absorption tower 62, an acid separator 67 is arranged above the filler portions 66, and a sulfur trioxide distribution mechanism 68 is arranged below the filler portions 66; the sulfur trioxide distribution mechanism 68 comprises a first cylinder 69 fixedly connected with the inner wall of the first absorption tower 61, a second cylinder 70 sleeved in the first cylinder 69, an upper annular plate 71 and a lower annular plate 72 which seal the upper and lower ends of the first cylinder 69 and the second cylinder 70, and a plurality of exhaust pipes 73 vertically arranged on the lower annular plate 72, wherein a cavity is formed among the first cylinder 69, the second cylinder 70, the upper annular plate 71 and the lower annular plate 72, the first cylinder 69 is connected with a second air inlet pipe 81 extending into the first absorption tower 61 so that the second air inlet pipe 81 is communicated with the cavity, the other end of the second air inlet pipe 81 is connected with an air outlet of the dryer 501, the upper end of the exhaust pipe 73 is communicated with the cavity, the lower end of the exhaust pipe is sealed, and a plurality of air outlet holes 74 are uniformly arranged on the pipe wall of the exhaust pipe 73; the upper parts of the first absorption tower 61 and the second absorption tower 62 are respectively provided with a demister 75, the top part of the first absorption tower 61 is provided with a gas transmission pipeline 76 which is communicated with a cavity part at the lower part of the second absorption tower 62, the top part of the second absorption tower 62 is provided with a tail gas discharge pipe 77, the lower parts of the first absorption tower 61 and the second absorption tower 62 are respectively connected with an acid pumping pipeline 78, the acid pumping pipeline 78 is provided with an acid liquor conveying pump 79 and a heat exchanger 80, and the outlet end of the acid pumping pipeline 78 is connected to the acid distributor 67; the sulfuric acid liquid outlet 65 is connected with an acid discharge pipeline communicated with the top of the sulfuric acid storage tank 63.
It also has the defoaming silk screen 219, and the center of defoaming silk screen 219 is upwards protruding, forms the hemisphere face, and defoaming silk screen 219 installs in tower shell 201 to be located spray set 203 top.
The outlet of the first inlet duct 204 is directed towards the center of the bottom of the column shell 201.
The outlet pipe 206, the outlet pipe 218, the water inlet manifold 213 and the first air inlet pipe 204 are respectively provided with a shut-off valve.
The lengths of the liquid accumulation grooves 209 are gradually decreased from the center to the outer diameter of the gas distribution plate 207.
The outer wall of the cylindrical riser mount 210 is provided with external threads, and the inner wall of the bottom of the riser 208 is provided with internal threads matched with the external threads.
The first cylinder 69, the second cylinder 70, the upper annular plate 71, the lower annular plate 72 and the exhaust tube 73 are all ceramic materials.
The diameter of the second cylinder 70 is three-fifths of the diameter of the first absorption tower 61 and the second absorption tower 62.
The sulfuric acid storage tank 63 is communicated with the lower parts of the first absorption tower 61 and the second absorption tower 62 through a pipeline and an infusion pump.
The working mode and principle are as follows: when the packed tower works, water is added onto the packing layer 205 through the spraying device 203 and flows downwards along a packing gap of the packing layer 205, acid gas (sulfur dioxide and sulfur trioxide) is filled into the tower shell 201 through the first air inlet pipeline 204, the gas is uniformly distributed at the bottom of the tower shell 201 because an air outlet of the first air inlet pipeline 204 faces the center of the bottom of the tower shell 201, then the gas rises upwards and enters the cylindrical riser mounting seat 210, then enters the riser 208 through the cylindrical riser mounting seat 210 and finally is discharged into the packing layer 205 through the vent holes 212 in the riser 208, the acid gas is fully neutralized and reacted with the water in the packing layer 205, and the reacted acid gas is discharged through the air outlet pipe 206. The acid liquor after reacting with the acid gas drops on the gas distribution plate 207 through the packing layer 205 and is collected in a group of liquid accumulation tanks 209, and is discharged to the bottom of the tower shell 201 through a group of liquid through holes 211, the acid liquor accumulated at the bottom of the tower shell 201 is discharged through a liquid outlet pipe 218 and enters a U-shaped pipe 216, heavier impurities fall into a settling pond 217 and are continuously settled, the impurity blockage of the liquid outlet pipe 218 by the impurities is avoided, and a blow-down valve is periodically opened to discharge the impurities in the settling pond 217. When the flow of the acid gas is large, a large amount of mist and foam can be generated at the top of the tower shell 201, most of mist and foam can be blocked and filtered through the defoaming wire net 219, the humidity of the discharged acid gas can be reduced, and the load of a dehumidifying device in a production line is reduced. The center of the defoaming screen 219 protrudes upwards to form a hemispherical surface, so that foam and mist are concentrated on the side of the defoaming screen 219 rather than the middle, and the carrying amount of liquid by acid gas is reduced. The packing layer 205 is placed on the liquid baffle 1213 of a group of draft tubes 208, the liquid baffle 1213 can prevent the liquid from entering from the vent 212, guarantee the air input, drip on the gas distribution plate 207, the liquid accumulation groove 209 plays a role of reducing the liquid holdup on the gas distribution plate 207, prevent the water surface from rising and submerging the vent 212. The set of vents 212 also serve to distribute the airflow.
The acid gas is absorbed by the filler to obtain sulfur dioxide gas, and then the sulfur dioxide gas enters a dryer 501 for drying and then is discharged into a conversion tower 502 for oxidation to obtain pure sulfur trioxide gas.
The sulfur dioxide gas and the oxygen after drying respectively through first gas pipeline 4 and second gas pipeline 5 get into gas distributor 9 in (because first gas pipeline 4 and second gas pipeline 5 reentry gas distributor 9 through steam conduit is inside again, sulfur dioxide gas and oxygen in gas distributor 9 are high temperature sulfur dioxide gas and oxygen this moment), the two mixes (steam heating jacket 3 heats to about 400 degrees centigrade) and places box 2 and pass through the export of gas distributor 9 catalyst in proper order and pass through gas outlet discharge sulfur trioxide on reaction box 1. The operation mode of the catalyst placing box 2 is as follows: the gas is discharged from the air outlets of the silk screen 6, the ceramic carrier 7 adhered with the catalyst and the loading box 8 in sequence.
Or, the dried and oxygen gas respectively enter the gas distributor 9 through the first gas pipeline 4 and the second gas pipeline 5 (because the first gas pipeline 4 and the second gas pipeline 5 enter the gas distributor 9 through the inside of the steam pipeline, at this time, the sulfur dioxide gas and the oxygen gas in the gas distributor 9 are both high-temperature sulfur dioxide gas and high-temperature oxygen gas), the two are mixed in the chamber of the gas distributor 9 (the steam heating jacket 3 is heated to about 400 ℃), and enter the catalyst placing box 2 at the uppermost layer of the group of catalyst placing boxes 2 through the outlet of the gas distributor 9, and are subjected to gas guiding through the group of upper triangular guide plates 11 and the group of lower triangular guide plates 12 to avoid the gas from directly blowing on the ceramic carrier 7 to cause spherical damage, then pass through the ceramic carrier 7, and finally pass through the gas outlet to perform the next catalyst placing box 2, and then discharged through a gas outlet of the reaction box body 1.
The method for producing the catalyst-bonded ceramic carrier 7 comprises:
first adhesion
Soaking the ceramic carrier 7 in PTFE emulsion and rolling to coat the powder catalyst;
second adhesion
Spraying PTFE emulsion on the surface of the ceramic carrier 7 subjected to the first adhesion, wherein the concentration of the PTFE emulsion is less than that of the PTFE emulsion used for the first adhesion, and then rolling and coating the powder catalyst again;
third time of adhesion
Spraying PTFE emulsion on the surface of the ceramic carrier 7 subjected to the second adhesion, wherein the concentration of the PTFE emulsion is less than that of the PTFE emulsion used for the second adhesion, and then airing;
drying process
And drying the ceramic carrier 7 adhered for the third time at the maximum temperature of 100-130 ℃, naturally cooling, and sealing for storage.
The acid making process of the acid making equipment comprises the following steps: concentrated sulfuric acid in a sulfuric acid storage tank 63 is conveyed to the lower parts of a first absorption tower 61 and a second absorption tower 62 through an infusion pump, a pipeline and a concentrated sulfuric acid inlet 64, sulfur trioxide gas discharged from a gas outlet on a reaction box body 1 enters the first absorption tower 61 from a sulfur trioxide distribution mechanism 68 on the lower part of the first absorption tower 61, then an acid liquor conveying pump 79 is started to convey acid to an acid distributor 67, tail gas absorbed by the first absorption tower 61 enters the second absorption tower 62 to be adsorbed through the sulfur trioxide distribution mechanism 68 again, sulfuric acid after the adsorption of the first absorption tower 61 and the second absorption tower 62 flows back to the sulfuric acid storage tank 63, and the sulfuric acid flows back to the first absorption tower 61 and the second absorption tower 62 to be circulated after being diluted by adding water. The sulfur trioxide distribution mechanism gives vent to anger through a plurality of exit holes 74 of evenly distributed on the pipe wall of blast pipe 73 for sulfur trioxide gas can the intensive dispersion, avoids agglomerating, thereby can be better in packing portion 66 absorbed, effectively improves sulfur trioxide's absorption efficiency. The utility model discloses an it is efficient that system acid device absorbs sulfur trioxide, does not contain sulfur trioxide gas in the tail gas after absorbing basically.
Claims (9)
1. A sulfuric acid regeneration system comprises a sulfur dioxide purification packed tower (500), a dryer (501), a conversion tower (502) and an acid making device (503) which are connected in sequence,
the sulfur dioxide purification packed tower (500) comprises a tower shell (201), a packing supporting plate (202), a spraying device (203), a first air inlet pipeline (204), a packing layer (205) and an impurity precipitation device, wherein an air outlet pipe (206) is arranged at the top of the tower shell (201), a liquid outlet pipe (218) is arranged at the bottom of the tower shell (201), the packing supporting plate (202) comprises a gas distribution plate (207) and a group of gas-lift pipes (208), a group of liquid accumulation tanks (209) are arranged on the gas distribution plate (207), a group of liquid through holes (211) are formed in the bottom of each liquid accumulation tank (209), a group of cylindrical gas-lift pipe mounting seats (210) are arranged between every two adjacent liquid accumulation tanks (209), a group of vent holes (212) are annularly and uniformly distributed on the upper pipe wall of each gas-lift pipe (208), a liquid baffle plate (1213) is arranged at the top of each gas-lift pipe (208), and the group of gas, the packing support plate (202) is arranged in the tower shell (201), the spraying device (203) comprises a water inlet main pipe (213) and a group of branch pipes (214), one end of the water inlet main pipe (213) is positioned in the tower shell (201), the other end of the water inlet main pipe is positioned outside the tower shell (201), the group of branch pipes (214) are communicated with the water inlet main pipe (213), the water inlet main pipe (213) is provided with a group of spray heads (215), the end parts of the group of branch pipes (214) are respectively provided with the spray heads (215), a packing installation area is formed between the spraying device (203) and the packing support plate (202), the packing layer (205) is arranged in the packing installation area, the air outlet end of the first air inlet pipe (204) is positioned in the tower shell (201) and below the packing support plate (202), the air inlet end of the first air inlet pipe (204) is positioned outside the tower shell (201), the impurity precipitation device comprises a U-shaped pipe (216), the inlet end of the U-shaped pipe (216) is communicated with the outlet end of the liquid outlet pipe (218), the bottom of the U-shaped pipe (216) is communicated with the sedimentation tank (217) through a pipeline, and the bottom of the sedimentation tank (217) is provided with a sewage discharge outlet;
an air outlet pipe (206) at the top of the tower shell (201) is connected with an air inlet of the dryer (501);
the conversion tower (502) comprises a reaction box body (1) and a group of catalyst placing boxes (2), a steam heating jacket (3) and a gas outlet are arranged on the reaction box body (1), a pair of steam inlets and a steam outlet are arranged on the steam heating jacket (3), a first steam pipeline and a second steam pipeline which are respectively communicated with the pair of steam inlets are arranged on the pair of steam inlets, the catalyst placing boxes (2) comprise a silk screen (6), a ceramic carrier (7) adhered with a catalyst and a loading box (8), a plurality of groups of air holes are formed in the bottom of the loading box (8), the ceramic carrier (7) adhered with the catalyst is positioned in the loading box (8), the silk screen (6) is detachably arranged on the top of the loading box (8), a gas distributor (9) and a group of catalyst placing boxes (2) are arranged at the top in the reaction box body (1), the gas distributor (9) and the group of catalyst placing boxes (2) are sequentially arranged from top to bottom, the gas outlet of the gas distributor (9) is positioned above the wire mesh (6) of the uppermost catalyst placing box (2) of the group of catalyst placing boxes (2), one ends of the first gas pipeline (4) and the second gas pipeline (5) respectively penetrate through the first steam pipeline and the second steam pipeline and are communicated with the gas inlet of the gas distributor (9), and the first gas pipeline (4) is connected with the gas outlet of the dryer (501);
the acid making equipment comprises a first absorption tower (61), a second absorption tower (62) and a sulfuric acid storage tank (63); concentrated sulfuric acid inlets (64) and sulfuric acid liquid outlets (65) are formed in the lower portions of the first absorption tower (61) and the second absorption tower (62), packing portions (66) are formed in the first absorption tower (61) and the second absorption tower (62), an acid distributor (67) is arranged above the packing portions (66), and a sulfur trioxide distribution mechanism (68) is arranged below the packing portions (66); sulfur trioxide distribution mechanism (68) include with first cylinder (69) of first absorption tower (61) inner wall rigid coupling, establish second cylinder (70) in first cylinder (69), with first cylinder (69) and second cylinder (70) about end confined go up annular plate (71) and lower annular plate (72) and vertical setting be in a plurality of blast pipes (73) on lower annular plate (72), form cavity portion between first cylinder (69), second cylinder (70), last annular plate (71) and lower annular plate (72), first cylinder (69) and stretch into second inlet duct (81) in first absorption tower (61) meet so that second inlet duct (81) with cavity portion communicates, and the other end of second inlet duct (81) is connected with the gas outlet of desicator (501), the upper end of blast pipe (73) with cavity portion communicates, The lower end is sealed, and a plurality of air outlet holes (74) are uniformly arranged on the pipe wall of the exhaust pipe (73); the upper parts of the first absorption tower (61) and the second absorption tower (62) are respectively provided with a demister (75), the top of the first absorption tower (61) is provided with a gas transmission pipeline (76) which is communicated with a cavity part at the lower part of the second absorption tower (62), the top of the second absorption tower (62) is provided with a tail gas discharge pipe (77), the lower parts of the first absorption tower (61) and the second absorption tower (62) are respectively connected with an acid pumping pipeline (78), an acid liquor conveying pump (79) and a heat exchanger (80) are arranged on the acid pumping pipeline (78), and the outlet end of the acid pumping pipeline (78) is connected to the acid distributor (67); the sulfuric acid liquid outlet (65) is connected with an acid discharge pipeline communicated with the top of the sulfuric acid storage tank (63).
2. A sulfuric acid regeneration system as claimed in claim 1, characterized in that it further comprises a defoaming screen (219), the center of the defoaming screen (219) is convex upward to form a hemispherical surface, and the defoaming screen (219) is installed in the tower shell (201) and above the spraying device (203).
3. A sulfuric acid regeneration system according to claim 1, characterized in that the outlet of the first inlet conduit (204) is directed towards the center of the bottom of the column shell (201).
4. A sulfuric acid regeneration system according to claim 1, characterized in that the outlet pipe (206), the outlet pipe (218), the inlet manifold (213) and the first inlet pipe (204) are provided with shut-off valves, respectively.
5. A sulfuric acid regeneration system according to claim 1, wherein the lengths of the plurality of liquid accumulation tanks (209) decrease in sequence from the center to the outer diameter of the gas distribution plate (207).
6. A sulfuric acid regeneration system as claimed in claim 1, wherein the cylindrical riser mount (210) has external threads on its outer wall and the riser (208) has internal threads on its bottom inner wall that mate with the external threads.
7. A sulfuric acid regeneration system according to claim 1, characterized in that the first cylinder (69), the second cylinder (70), the upper annular plate (71), the lower annular plate (72) and the exhaust pipe (73) are of ceramic material.
8. A sulfuric acid regeneration system according to claim 1, characterized in that the diameter of the second cylinder (70) is three fifths of the diameter of the first absorption tower (61) and the second absorption tower (62).
9. A sulfuric acid regeneration system according to claim 1, characterized in that said sulfuric acid storage tank (63) is communicated with the lower portions of the first absorption tower (61) and the second absorption tower (62) through a pipe and an infusion pump.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921557247.8U CN210528472U (en) | 2019-09-19 | 2019-09-19 | Sulfuric acid regeneration system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201921557247.8U CN210528472U (en) | 2019-09-19 | 2019-09-19 | Sulfuric acid regeneration system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112316672A (en) * | 2020-11-05 | 2021-02-05 | 中盐昆山有限公司 | Washing tower for filtering tail gas |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112316672A (en) * | 2020-11-05 | 2021-02-05 | 中盐昆山有限公司 | Washing tower for filtering tail gas |
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Denomination of utility model: A sulfuric acid regeneration system Granted publication date: 20200515 Pledgee: Bank of China Limited by Share Ltd. Jingmen branch Pledgor: JINMEN CITY YUCHU CHEMICAL CO.,LTD. Registration number: Y2024980027408 |
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