CN201408157Y - Density and pH valve measuring device for wet flue gas desulfurization slurry - Google Patents
Density and pH valve measuring device for wet flue gas desulfurization slurry Download PDFInfo
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- CN201408157Y CN201408157Y CN2009200138730U CN200920013873U CN201408157Y CN 201408157 Y CN201408157 Y CN 201408157Y CN 2009200138730 U CN2009200138730 U CN 2009200138730U CN 200920013873 U CN200920013873 U CN 200920013873U CN 201408157 Y CN201408157 Y CN 201408157Y
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- density
- slurries
- flue gas
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Abstract
The utility model relates to a density and pH valve measuring device for wet flue gas desulfurization slurry, which overcomes the shortcomings of the prior art that a device stops work because a density meter and a PH meter are blocked easily and the like. The device comprises a main pipeline, a density meter, a pH meter, a return pipeline as well as a connecting flange thereof and a bend pipe, and is technically characterized in that the main pipeline is provided with branch pipes, the return pipeline and a butt clamp electric valve, a diaphragm valve and a supporting cylinder which are sequentially communicated via the branch pipes constitute a slurry circulation loop, the side walls of the branch pipes and the supporting cylinder are provided with communicated flush pipes, the side walls of the branch pipes are communicated with the density meter, and the pH meter is arranged in the supporting cylinder. The device has reasonable structure design and can ensure that the density meter and the pH meter can operate within the range of pipeline flow rate permitted by the meters so as to be flushed and maintained on line, the accuracy of the measurement value of the desulfurization slurry is significantly improved so as to be favorable for the desulfurization and standard discharge of the flue gas and the operation stability of the equipment, the problem of the shutdown of desulfurization equipment is fundamentally eliminated, and the service life of the meters is prolonged.
Description
Technical field
The utility model relates to a kind of gypsum slurries in the wet flue gas desulfurizer trunk line, detecting instrument of lime stone slurry of being used for, particularly a kind of serous fluid processed by wet flue gas desulfurization density, pH value measurement mechanism of measuring accurately, being convenient to online flushing and maintenance.
Background technology
At present, in the wet flue gas desulfurizer operational process, for guaranteeing desulfurizer reliability of operation and flue gas desulfurization effect, must detect the gypsum slurries that the flue gas desulfurization effect is played a decisive role in the desulfurizer, the density and the pH value of lime stone slurry.The densitometer that existing detecting instrument adopts is directly installed on the trunk line separately; pH meter is installed on the absorption tower; cause density to take into account the damage of pH meter easily, influence its serviceable life and usability, damage the problem that causes a whole set of desulfurizer to be shut down in case exist density to take into account pH meter.Because densitometer and pH meter belong to exact instrument, want to make measured value more accurate, must carry out periodic flushing and maintenance to it, so that keep having suitable slurries speed in the desulfurizer pipeline, improve operation stability, prevent fault.Existing desulfurizer since densitometer be directly installed on separately on the trunk line, can't accurately measure and controlling plumbing fixtures in slurries speed in the scope that instrument allows, can not realize online flushing and maintenance, make its lost of life; And pH meter is installed on the absorption tower, and its installation pipeline is mobile poor, causes pipeline obstruction easily, thereby influences the accuracy that the pH value is measured.So, need exploitation to be fit to densitometer, the pH value measurement mechanism of the wet flue gas desulfurizer of China's actual conditions at present.
The utility model content
The purpose of this utility model provides a kind of serous fluid processed by wet flue gas desulfurization density; the pH value measurement mechanism; the densitometer and the pH meter that have solved existing wet flue gas desulfurizer existence can not be realized online flushing; easily block; influence measuring accuracy; cause defectives such as equipment downtime; its reasonable in design; can guarantee that density takes into account pH meter and move in the pipe flow speed scope that instrument allows; be convenient to online flushing and maintenance; significantly improve accurate measurement to the desulfurization slurry detected value; be beneficial to flue gas desulfurization qualified discharge and stable equipment operation, fundamentally eliminate the problem that sweetener is shut down, prolonged the serviceable life of instrument simultaneously.
The technical scheme that the utility model adopted is: this serous fluid processed by wet flue gas desulfurization density, the pH value measurement mechanism comprises the conveying gypsum slurries, the densitometer of the trunk line of lime stone slurry and measurement slurries, pH meter, tested slurries are sent into reflux line and the joint flange and the bend pipe of slurries baffle-box, its technical essential is: on the described trunk line take-off pipe is set, and by described take-off pipe and described joint flange, bend pipe carry out that order is communicated with to the folder motorized valve, diaphragm valve and support tube and described reflux line are formed the slurries closed circuit, described take-off pipe to the folder motorized valve, the wash tub pipe of connection is set between the diaphragm valve, sidewall at described take-off pipe is communicated with described densitometer, the wash tub pipe of connection is set on described support tube sidewall, and described pH meter is arranged in the support tube.
Reflux line in the described slurries closed circuit is communicated with two groups of diaphragm valves and pH meter support tube respectively, and utilizes threeway and have densitometric described take-off pipe and be communicated with.
Advantage and the good effect that the utlity model has are: because the utility model is in same set of slurries closed circuit, by take-off pipe and joint flange carry out that order is communicated with to folder motorized valve, diaphragm valve and support tube, packing density meter, pH meter, so its reasonable in design, can not only guarantee that density takes into account pH meter and move in the pipe flow speed scope that instrument allows, and it is little to take up room, and easy operating control is convenient to safeguard and maintenance.In addition; because of take-off pipe to the folder motorized valve; the wash tub pipe of connection is set between the diaphragm valve; the wash tub pipe of connection is set on pH meter support tube sidewall; therefore be readily embodied in line flushing and maintenance; can significantly improve accurate measurement to the desulfurization slurry detected value; reduced the whole accident frequency of shutting down of wet flue gas desulfurizer; be beneficial to flue gas desulfurization qualified discharge and stable equipment operation; can not realize online flushing from the densitometer and the pH meter that have solved existing wet flue gas desulfurizer existence at all; easily block; influence measuring accuracy, cause defectives such as equipment downtime, prolonged the serviceable life of instrument simultaneously.
Description of drawings
Below in conjunction with accompanying drawing the utility model is further described.
Sequence number explanation among the figure: 1pH meter, 2 diaphragm valves, 3 wash tub pipes, the 4 pairs of folder motorized valves, 5 densitometers, 6 threeways, 7 trunk lines, 8 support tubes, 9 joint flanges, 10 reflux lines.
Embodiment
Describe concrete structure of the present utility model in detail according to Fig. 1.This serous fluid processed by wet flue gas desulfurization density, pH value measurement mechanism comprise trunk line 7 and measure the densitometer (mass flowmeter/densitometer) 5 of slurries, pH meter 1, reflux line 10 and a plurality of joint flange 9, diaphragm valve 2 and bend pipe are to parts such as folder motorized valve 4 and support tubes 8.Wherein carry on the trunk line 7 of gypsum slurries, lime stone slurry take-off pipe is set, and will carry out order to folder motorized valve 4, diaphragm valve 2 and support tube 8 by take-off pipe and joint flange 9, bend pipe and be communicated with, then with the reflux line 10 composition slurries closed circuits of tested slurries being sent into the slurries baffle-box.Diaphragm valve 2 is for breaking down at densitometer or pH meter, safeguards and closes that the localized branches pipeline is provided with when overhauling.Take-off pipe to folder motorized valve 4, diaphragm valve 2 between the wash tub pipe 3 of connection is set.Be communicated with densitometer 5 at the sidewall of take-off pipe, gypsum slurries, the lime stone slurry of flowing through in it carried out the measurement of serum density, connect wash-down water with wash tub pipe 3 interfaces simultaneously diaphragm valve 2, the take-off pipe etc. that has a densitometer 5 are carried out online flushing.The wash tub pipe 3 of connection is set on support tube 8 sidewalls, connects wash-down water with wash tub pipe 3 interfaces pH meter is carried out online flushing.PH meter 1 is arranged in the support tube 8, and the gypsum slurries in it of flowing through, the pH value of lime stone slurry are measured.PH meter 1 can be provided with two, also can be provided with one.Normal operation for not overslaugh slurries closed circuit, can be with the reflux line in the slurries closed circuit 10 and two groups of independently shunt of diaphragm valve 2 and support tube 8 compositions that have pH meter 1 separately, be communicated with respectively, and utilize threeway 6 that two shunt are communicated with the take-off pipe that has densitometer 5.When single pH meter 1 breaks down when need removing, can close and this side corresponding diaphragm valve 2 along separate routes, this pH meter 1 is safeguarded and keeped in repair.
The course of work is as follows: when gypsum slurries or lime stone slurry the time, enter the take-off pipe that is provided with on the trunk line 7 immediately by trunk line 7, again through to folder motorized valve 4, diaphragm valve 2, arrive densitometer 5 and carry out the measurement of serum density; Enter diaphragm valve 2, pH meter support 8, pH meter 1 respectively by threeway 6 then, slurry pH value is measured.Tested slurries are sent into the gypsum slurries baffle-box by reflux line 10.Adopt conventional control technology can utilize the interface by wash tub pipe 3 towards Xian Shui, respectively to diaphragm valve 2, have the take-off pipe of densitometer 5 or pH meter carried out online flushing.
Claims (2)
1, a kind of serous fluid processed by wet flue gas desulfurization density, the pH value measurement mechanism, comprise the conveying gypsum slurries, the densitometer of the trunk line of lime stone slurry and measurement slurries, pH meter, tested slurries are sent into the reflux line and the joint flange thereof of slurries baffle-box, it is characterized in that: on the described trunk line take-off pipe is set, and by described take-off pipe and described joint flange, bend pipe carry out that order is communicated with to the folder motorized valve, diaphragm valve and support tube and described reflux line are formed the slurries closed circuit, described take-off pipe to the folder motorized valve, the wash tub pipe of connection is set between the diaphragm valve, sidewall at described take-off pipe is communicated with described densitometer, the wash tub pipe of connection is set on described support tube sidewall, and described pH meter is arranged in the support tube.
2, serous fluid processed by wet flue gas desulfurization density according to claim 1, pH value measurement mechanism, it is characterized in that: the reflux line in the described slurries closed circuit is communicated with two groups of diaphragm valves and pH meter support tube respectively, and utilizes threeway and have densitometric described take-off pipe and be communicated with.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN2009200138730U CN201408157Y (en) | 2009-05-22 | 2009-05-22 | Density and pH valve measuring device for wet flue gas desulfurization slurry |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN2009200138730U CN201408157Y (en) | 2009-05-22 | 2009-05-22 | Density and pH valve measuring device for wet flue gas desulfurization slurry |
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CN201408157Y true CN201408157Y (en) | 2010-02-17 |
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CN2009200138730U Expired - Fee Related CN201408157Y (en) | 2009-05-22 | 2009-05-22 | Density and pH valve measuring device for wet flue gas desulfurization slurry |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102012352A (en) * | 2010-10-22 | 2011-04-13 | 武汉东湖高新集团股份有限公司 | Device for measuring density and pH value of slurry |
CN102489144A (en) * | 2011-12-23 | 2012-06-13 | 武汉光谷环保科技股份有限公司 | Measure apparatus of flue gas desulphurization absorbing tower, slurry pH meter and densitometer by using wet method and its method |
-
2009
- 2009-05-22 CN CN2009200138730U patent/CN201408157Y/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102012352A (en) * | 2010-10-22 | 2011-04-13 | 武汉东湖高新集团股份有限公司 | Device for measuring density and pH value of slurry |
CN102012352B (en) * | 2010-10-22 | 2012-01-18 | 武汉东湖高新集团股份有限公司 | Device for measuring density and pH value of slurry |
CN102489144A (en) * | 2011-12-23 | 2012-06-13 | 武汉光谷环保科技股份有限公司 | Measure apparatus of flue gas desulphurization absorbing tower, slurry pH meter and densitometer by using wet method and its method |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100217 Termination date: 20170522 |
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CF01 | Termination of patent right due to non-payment of annual fee |