CN205127767U - Backward flow formula bromine gas absorption tower - Google Patents

Backward flow formula bromine gas absorption tower Download PDF

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Publication number
CN205127767U
CN205127767U CN201520895883.7U CN201520895883U CN205127767U CN 205127767 U CN205127767 U CN 205127767U CN 201520895883 U CN201520895883 U CN 201520895883U CN 205127767 U CN205127767 U CN 205127767U
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China
Prior art keywords
liquid pump
drawing liquid
bromine gas
gas absorption
absorption tower
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CN201520895883.7U
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Chinese (zh)
Inventor
苏长流
陈丰
孙阳
朱天武
王信义
王进利
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Linhai Jianxin Chemical Co Ltd
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Linhai Jianxin Chemical Co Ltd
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Abstract

The utility model discloses a backward flow formula bromine gas absorption tower is aimed at providing in the bromine gas absorption tower, and it has the function that prevents the drawing liquid pump and damage because of the jam, and its technical scheme main points are: including the tower body, locate the jar body of tower body lower part, be equipped with the output tube that is used for inputing bromine gas's input tube and is used for discharging bromine solution on the jar body, be equipped with back flow and first valve on the output tube, be equipped with the second valve on the back flow, the junction of output tube and back flow is equipped with the drawing liquid pump, is located to be equipped with the filter plate on the output tube of drawing liquid pump intake department, still be equipped with the sediment tube on the output tube, the filter plate is located between sediment tube and the drawing liquid pump intake, be equipped with the third valve on the sediment tube.

Description

Reverse-flow type bromine gas absorption tower
Technical field
The utility model relates to a kind of bromine gas absorption tower, and more particularly, it relates to a kind of reverse-flow type bromine gas absorption tower, and it has the function preventing drawing liquid pump from damaging because of blocking.
Background technology
Bromine gas absorption tower is a kind of tower for obtained bromine solutions, bromine gas obtains bromine solutions by physical dissolution, usual use methanol aqueous solution is as the absorbing liquid of bromine gas, reverse-flow type bromine gas absorption tower mainly comprises tower body, be located at the tank body of tower body bottom, tower body is communicated with tank body, tank body can be provided with the input pipe passing into bromine gas, tank base is provided with the efferent duct of discharging bromine solutions, efferent duct is also provided with return duct, one end of return duct passes into tower body inside, drawing liquid pump is provided with in the junction of efferent duct and return duct, both liquid in efferent duct can have been made to export fast by drawing liquid pump, also liquid can be made to be back to tower body from return duct, the setting in this loop substantially increases the utilization rate that bromine solutions prepares Raw, and enhance productivity.
But there is certain defect in traditional reverse-flow type bromine gas absorption tower; filler chip in tower body can fall into tank body; also a small amount of sediment can be there is in tank body; when drawing liquid pump twitches bromine solutions flowing; the sediments such as filler chip will flow along with solution; the normal work affecting pump is entered in pump in order to prevent sediment; usual meeting arranges filter plate at pumping hole place and filters; but sediment accumulates in filter plate place easily causes filter plate to block inefficacy; namely produce pumping hole blocking, cause pump to lack liquid, even aneroid; there is the phenomenon of dry grinding, be easy to like this cause pump to damage.
Utility model content
For the deficiency that prior art exists, the purpose of this utility model is to provide a kind of reverse-flow type bromine gas absorption tower, and it has the function preventing drawing liquid pump from damaging because of blocking.
For achieving the above object, the utility model provides following technical scheme: a kind of reverse-flow type bromine gas absorption tower, comprise tower body, be located at the tank body of tower body bottom, described tank body is provided with the input pipe for inputting bromine gas and the efferent duct for discharging bromine solutions, described efferent duct is provided with return duct and the first valve, return duct is provided with the second valve, the junction of described efferent duct and return duct is provided with drawing liquid pump, the efferent duct being positioned at drawing liquid pump porch is provided with filter plate, described efferent duct is also provided with sediment tube, described filter plate is between sediment tube and drawing liquid pump entrance, described sediment tube is provided with the 3rd valve.
Preferably, the translucent polyvinylidene fluoride material of described sediment tube is made.
Preferably, described drawing liquid pump is magnetic drive pump.
Preferably, one end that described return duct passes into tower body is provided with spray head.
Preferably, the material of described efferent duct and return duct is polyvinylidene fluoride.
Compared with prior art, the beneficial effects of the utility model are: described efferent duct is also provided with sediment tube, described filter plate is between sediment tube and drawing liquid pump entrance, described sediment tube is provided with the 3rd valve, filter plate is arranged on drawing liquid pump porch and can effectively prevents from sediment from entering in drawing liquid pump causing drawing liquid pump to damage, because sediment can be piled up by filter plate place, sediment is piled up for a long time and is easily caused drawing liquid pump entrance to block, therefore efferent duct before filter plate connects a sediment tube, sediment Direct precipitation can not be blocked in the entrance of drawing liquid pump in sediment tube, can effectively prevent drawing liquid pump from damaging because of blocking, simultaneously can not timing sediment be discharged by the 3rd valve, prevent precipitate bulk too much.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model reverse-flow type bromine gas absorption tower embodiment;
Fig. 2 is the enlarged drawing in B portion in Fig. 1;
Fig. 3 is the side-looking structural representation of the utility model reverse-flow type bromine gas absorption tower embodiment;
Fig. 4 be the utility model reverse-flow type bromine gas absorption tower embodiment A-A to partial sectional view.
Reference numeral: 1, tower body; 2, tank body; 3, input pipe; 4, efferent duct; 5, return duct; 6, the first valve; 7, the second valve; 8, the 3rd valve; 9, spray head; 10, drawing liquid pump; 11, filter plate; 12, sediment tube; 13, the 4th valve.
Detailed description of the invention
For making the object of the utility model embodiment, technical scheme and advantage clearly, the utility model reverse-flow type bromine gas absorption tower embodiment being done describe clearly and completely further below with reference to accompanying drawings.Obviously, described embodiment is section Example of the present utility model, instead of whole embodiments.Based on described embodiment of the present utility model, the every other embodiment that those of ordinary skill in the art obtain under without the need to the prerequisite of creative work, all belongs to the scope of the utility model protection.
As accompanying drawing 1, shown in 2, reverse-flow type bromine gas absorption tower comprises tower body 1, be located at the tank body 2 of tower body 1 bottom, tower body 1 is connected with tank body 2, described tank body 2 is provided with the input pipe 3 for inputting bromine gas and the efferent duct 4 for discharging bromine solutions, by input pipe 3, a certain amount of methanol aqueous solution is input to tank body 2 inside, again bromine gas being passed into tank body 2 inside by input pipe 3 makes bromine gas be dissolved in the methanol aqueous solution of tank body 2 inside, described efferent duct 4 is provided with return duct 5, one end of return duct 5 passes into tower body 1 inside, described efferent duct 4 is provided with the first valve 6, return duct 5 is provided with the second valve 7, the junction of described efferent duct 4 and return duct 5 is provided with the drawing liquid pump 10 for twitching bromine solutions, return duct 5 is again back in tank body 2 for the bromine solutions that the concentration that exported by efferent duct 4 is not up to standard and mixes, drawing liquid pump 10 provides power to the flowing of liquid in efferent duct 4 and return duct 5, in the present embodiment, return duct 5 is between drawing liquid pump 10 exit and the first valve 6, the form of liquid output and backflow is as follows: during backflow, close the first valve 6 on efferent duct 4, open the second valve 7 on return duct 5, liquid is back in tank body 2 from return duct 5, during output liquid, open the first valve 6 on efferent duct 4, close the second valve 7 on return duct 5, liquid outputs to next station from efferent duct 4.The efferent duct 4 being simultaneously positioned at drawing liquid pump 10 porch is provided with the filter plate 11 for preventing drawing liquid pump 10 from blocking, for the sediment tube 12 of collecting precipitation thing, described filter plate 11 is between sediment tube 12 and drawing liquid pump 10 entrance, described sediment tube 12 is provided with for discharging sedimentary 3rd valve 8, filter plate 11 is arranged on drawing liquid pump 10 porch and can effectively prevents from sediment from entering in drawing liquid pump 10 causing drawing liquid pump 10 to damage, due to filter plate 11, sediment can be piled up by place, sediment is piled up for a long time and is easily caused drawing liquid pump 10 entrance to block, therefore efferent duct 4 before filter plate 11 connects a sediment tube 12, sediment Direct precipitation can not be blocked in the entrance of drawing liquid pump 10 in sediment tube 12, can effectively prevent drawing liquid pump 10 from damaging because of blocking, simultaneously can not timing sediment be discharged by the 3rd valve 8, prevent precipitate bulk too much, efferent duct 4 is also provided with the 4th valve 13, before 4th valve 13 is located at sediment tube 12, when needing to discharge sediment tube 12 sediment, bromine solutions after closing the 4th valve 13 in tank body 2 would not flow into efferent duct 4, now can open the 3rd valve 8 waste discharge thing smoothly.
The translucent polyvinylidene fluoride material of described sediment tube 12 is made, polyvinylidene fluoride is not only trnaslucent materials and has good resistance to bromine corrosive nature, the sediment state in sediment tube 12 can be observed by translucent sediment tube 12 at any time, valve can be opened when sediment arrives a certain amount of and discharge.
Described drawing liquid pump is magnetic drive pump, magnetic drive pump is formed primarily of pump head, magnetic driver, motor, can for the magnetic drive pump described in patent No. CN203394770U, when motor drives outer magnet rotor to rotate, magnetic field energy penetrates air-gap and namagnetic substance, in drive is connected with impeller, magnet rotor makes synchronous rotary, realize the contactless synchronous transmission of power, the movable sealing structure easily revealed is converted into the static seal structure of zero leakage, because pump shaft, interior magnet rotor are completely closed by the pump housing, separation sleeve, thus thoroughly solve leakage, emit the problems such as liquid.
As accompanying drawing 3, shown in 4, one end that return duct 5 passes into tower body 1 is provided with spray head 9, concentration bromine solutions not up to standard flows on tower body 1 by return duct 5, usual bromine gas is understood some and is risen, mix more fully to allow the solution of backflow and the bromine gas of rising, adopt spray head 9, make backflow solution spraying and under, effectively increase the contact area of reflux solution and bromine gas, bromine gas is better dissolved in reflux solution, the material of described efferent duct 4 and return duct 5 is polyvinylidene fluoride, polyvinylidene fluoride has very strong impact resistance simultaneously, heat-resisting quantity is strong, be suitable as circulating line to use, increase the service life of pipeline, meanwhile, the color of bromine solutions can be observed by translucent efferent duct 4, by comparison color can judge bromine gas be dissolved in methanol-water easily in state, control bromine solutions concentration, this structure overcomes traditionally by means of only controlling the proportioning of bromine gas and methanol aqueous solution to control bromine liquid concentration, its concentration controls inaccurate problem, avoid simultaneously and offer the problem that visor affects tank body 2 sealing and tank body 2 intensity on tank body 2.
The above is only exemplary embodiment of the present utility model, but not for limiting protection domain of the present utility model, protection domain of the present utility model is determined by appended claim.

Claims (5)

1. a reverse-flow type bromine gas absorption tower, comprise tower body, be located at the tank body of tower body bottom, described tank body is provided with the input pipe for inputting bromine gas and the efferent duct for discharging bromine solutions, described efferent duct is provided with return duct and the first valve, return duct is provided with the second valve, the junction of described efferent duct and return duct is provided with drawing liquid pump, the efferent duct being positioned at drawing liquid pump porch is provided with filter plate, it is characterized in that: described efferent duct is also provided with sediment tube, described filter plate is between sediment tube and drawing liquid pump entrance, and described sediment tube is provided with the 3rd valve.
2. reverse-flow type bromine gas absorption tower according to claim 1, is characterized in that: the translucent polyvinylidene fluoride material of described sediment tube is made.
3. reverse-flow type bromine gas absorption tower according to claim 2, is characterized in that: described drawing liquid pump is magnetic drive pump.
4. reverse-flow type bromine gas absorption tower according to claim 2, is characterized in that: one end that described return duct passes into tower body is provided with spray head.
5. reverse-flow type bromine gas absorption tower according to claim 4, is characterized in that: the material of described efferent duct and return duct is polyvinylidene fluoride.
CN201520895883.7U 2015-11-11 2015-11-11 Backward flow formula bromine gas absorption tower Active CN205127767U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201520895883.7U CN205127767U (en) 2015-11-11 2015-11-11 Backward flow formula bromine gas absorption tower

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201520895883.7U CN205127767U (en) 2015-11-11 2015-11-11 Backward flow formula bromine gas absorption tower

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CN205127767U true CN205127767U (en) 2016-04-06

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112717870A (en) * 2020-12-04 2021-04-30 张荷友 Anti-blocking device for tubular reactor

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112717870A (en) * 2020-12-04 2021-04-30 张荷友 Anti-blocking device for tubular reactor

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