CN106123981A - In a kind of reaction tower, waste water flows through filler speed monitoring monitoring system - Google Patents
In a kind of reaction tower, waste water flows through filler speed monitoring monitoring system Download PDFInfo
- Publication number
- CN106123981A CN106123981A CN201610442747.1A CN201610442747A CN106123981A CN 106123981 A CN106123981 A CN 106123981A CN 201610442747 A CN201610442747 A CN 201610442747A CN 106123981 A CN106123981 A CN 106123981A
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- Prior art keywords
- sensor
- probe
- plug
- fluid
- reaction
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- 238000006243 chemical reaction Methods 0.000 title claims abstract description 58
- 238000012544 monitoring process Methods 0.000 title claims abstract description 32
- 239000000945 filler Substances 0.000 title claims abstract description 18
- 239000002351 wastewater Substances 0.000 title claims abstract description 18
- 239000000523 sample Substances 0.000 claims abstract description 46
- 239000012530 fluid Substances 0.000 claims abstract description 45
- 238000012856 packing Methods 0.000 claims abstract description 20
- 239000000463 material Substances 0.000 claims abstract description 11
- 238000000034 method Methods 0.000 claims description 9
- 238000012545 processing Methods 0.000 claims description 7
- 238000007789 sealing Methods 0.000 claims description 5
- 230000000694 effects Effects 0.000 claims description 3
- 238000005259 measurement Methods 0.000 claims description 3
- 238000007639 printing Methods 0.000 claims description 3
- 230000002463 transducing effect Effects 0.000 claims 1
- 239000007788 liquid Substances 0.000 description 7
- 239000007789 gas Substances 0.000 description 5
- 239000002912 waste gas Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 1
- 206010067265 Heterotaxia Diseases 0.000 description 1
- 208000002128 Heterotaxy Syndrome Diseases 0.000 description 1
- 208000011934 Situs ambiguus Diseases 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006757 chemical reactions by type Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 238000002372 labelling Methods 0.000 description 1
- 229950000845 politef Drugs 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 230000032258 transport Effects 0.000 description 1
- 201000006869 visceral heterotaxy Diseases 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01F—MEASURING VOLUME, VOLUME FLOW, MASS FLOW OR LIQUID LEVEL; METERING BY VOLUME
- G01F1/00—Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through a meter in a continuous flow
- G01F1/66—Measuring the volume flow or mass flow of fluid or fluent solid material wherein the fluid passes through a meter in a continuous flow by measuring frequency, phase shift or propagation time of electromagnetic or other waves, e.g. using ultrasonic flowmeters
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0006—Controlling or regulating processes
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- Chemical & Material Sciences (AREA)
- Physics & Mathematics (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electromagnetism (AREA)
- Fluid Mechanics (AREA)
- General Physics & Mathematics (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
nullIn the invention discloses a kind of reaction tower, waste water flows through filler speed monitoring monitoring system，Including reaction tower，Packing layer it is provided with in reaction tower，Wherein on reaction tower tower body, it is provided with Fluid A Inlet，Fluid B inlet，Valve sensor A it is provided with at Fluid A Inlet，Valve sensor B it is provided with at Fluid B inlet，It is respectively provided with plug in sensor A in packing layer upper end，Plug in sensor A is provided with plug in sensor probe A，It is respectively provided with plug in sensor B in packing layer upper end，Plug in sensor B is provided with plug in sensor probe B，Probe A and probe B can sense the flow velocity of mixing object，In one reaction tower of the present invention, waste water flows through filler speed monitoring monitoring system，Arrange simple，Material monitoring is convenient，Ensure that material reaction is complete，Litter discharge is up to state standards.
Description
Technical field
The present invention relates to field of Environment Protection, particularly relate to waste water in a kind of reaction tower and flow through filler speed monitoring monitoring system
System.
Background technology
At chemical industry, field of Environment Protection, reaction tower is widely used, and reaction tower is also referred to as purifying column, packed tower, leads in packed tower
Often having two kinds or two or more media absorbs in tower, chemical reaction, medium generally includes two classes, liquid and liquid
Reaction class, gas and liquid reactions class, such as waste water in environmental protection industry (epi), the process of waste gas, in order to increase the abundant of reacting gas,
Being provided with Pall ring in reaction tower tower body, altogether strategic point ring, Raschig ring, these fillers use fluorine plastic product to make, corrosion-resistant, the most often
Filler be politef, and in Pall ring filler add PPL.
No matter the diameter of existing reaction tower tower and height, being provided with packing layer in reaction tower, bed stuffing height is general
Only it is by estimation, there is no exact height, in using, a number of packing ring, such as Pall ring are joined packing layer, filler
Situs ambiguus, number is indefinite, and employing is toppled over mode and added, and along with country is to the attention in terms of environmental protection, some reaction towers give up
Water processes or exhaust-gas treatment standard-required is more and more higher, and country is to waste gas, and discharge of wastewater is more strict, existing packed tower because of
For spray rate, liquid internal flow exchange velocity occurs inconsistent, it is easy to waste gas occur, and waste water discharges phenomenon the most up to standard.
To this end, waste water flows through filler speed monitoring monitoring system in the invention provides a kind of reaction tower so that material exists
Fully react in packed tower, and through strict test, could be waste gas, waste water is discharged outside tower body.
Summary of the invention
The technical problem that present invention mainly solves is to provide waste water in a kind of reaction tower and flows through filler speed monitoring monitoring system
System, it is possible to different liquids or the flowing velocity of gas in monitoring reaction tower, so that material reaction mix homogeneously so that useless
Gas thing emission compliance, and the monitoring system that the present invention provides, be different from traditional mechanical measuring instrument pattern, and this patent uses
Be ultrasonic flow observing and controlling technology.
In described a kind of reaction tower, waste water flows through filler speed monitoring monitoring system, including reaction tower, in reaction tower
Being provided with packing layer, be wherein provided with Fluid A Inlet, Fluid B inlet on reaction tower tower body, wherein fluid A transports from top to bottom
Dynamic, fluid B moves from bottom to top, wherein fluid A, and fluid B is liquid or gaseous state.
At Fluid A Inlet, be provided with valve sensor A, be provided with at Fluid B inlet valve sensor B, fluid A from
On move downward, fluid B moves from bottom to top, through packing layer, reacts in packing layer.
In course of reaction, there is the conversion of speed, under normal condition, fluid keeps a kind of standard state of flow, thing
Material reaction is the most abundant, and a certain fluid is vulgar or exceeds the speed limit, and arises that cutout or turbulent flow so that react insufficient.
It is respectively provided with plug in sensor A in packing layer upper end, plug in sensor A is provided with plug-in type sensing
Device probe A, is respectively provided with plug in sensor B in packing layer upper end, is provided with plug-in type sensing on plug in sensor B
Device probe B, probe A and probe B can sense the flow velocity of mixing object.
A kind of optimal technical scheme, so that the stablizing of probe A and probe B measurement flow rate, at plug in sensor A,
It is connected to cowling panel so that measure accurately on plug in sensor B.
At work, the fluid A of valve sensor A moves downward, and the flow velocity in probe A should be valve sensor A's
Flow velocity low, concrete coefficient is the process coefficient of real reaction, as being set to a1, a1 equal to the flow velocity of probe A divided by valve
The flow velocity of door sensor A；The fluid B of valve sensor B moves upward, and the flow velocity in probe B should be than the stream of valve sensor B
Fast is low, and concrete coefficient is the process coefficient of real reaction, with the flow velocity of probe B divided by the flow velocity at valve sensor B, arranges
For b1.
Sealed by sealing ring between plug in sensor A and plug in sensor B and reaction tower, valve sensor A, valve
Door sensor B, probe A, probe B is connected with supersonic flow amount controller by data wire respectively, first, and valve sensor A, valve
Door sensor B, probe A, probe B is connected with signal processing module, the data signal gathered through processing, is then attached to surpass
Raw wave transducer, and have children outside the state plan wave transducer and filter through wave filter, it is then passed through amplifier and is amplified, and signal is passed
Being passed to oscillograph, oscillograph is connected to host computer, and host computer uses computer processor structure, and host computer enters the data gathered
Row compares calculating.Numerical value relatively and initial parameter contrast, if the change of parameter occurrence scope, host computer passes through data
Line is connected to control switch, under the effect controlling switch, controls fluid A and the speed of fluid B respectively so that reaction to
Steadily direction is run.
A kind of optimal technical scheme, is connected to printer on host computer, it is possible to data are carried out arranging printing, it is simple to thing
The analysis of material reaction.
The invention has the beneficial effects as follows: in one reaction tower of the present invention, waste water flows through filler speed monitoring monitoring system, if
Putting simple, material monitoring is convenient, it is ensured that material reaction is complete so that Litter discharge is up to state standards, and protects environment.
Accompanying drawing explanation
Fig. 1 is the structural representation that waste water flows through filler speed monitoring monitoring system in a kind of reaction tower of the present invention；
In accompanying drawing, the labelling of each parts is as follows:
1 is Fluid A Inlet, and 2 is Fluid B inlet, and 3 is packing layer, and 4 is valve sensor A, and 5 is valve sensor B, and 6 for inserting
Formula sensors A, 7 is plug in sensor probe A, and 8 is sealing ring A, and 6 ' is plug in sensor B, and 7 ' is plug in sensor
Probe B, 8 ' is sealing ring B, and 9 is signal processing module, and 10 is excusing from death wave transducer, and 11 is wave filter, and 12 is amplifier, 13
Being transferred to oscillograph for signal, 14 is host computer, and 15 for controlling switch.
Detailed description of the invention
Below in conjunction with the accompanying drawings presently preferred embodiments of the present invention is described in detail, so that advantages and features of the invention energy
It is easier to be readily appreciated by one skilled in the art, thus protection scope of the present invention is made apparent clear and definite defining.
Referring to Fig. 1, the embodiment of the present invention includes:
In described a kind of reaction tower, waste water flows through filler speed monitoring monitoring system, including reaction tower, arranges in reaction tower
Packing layer, is wherein provided with Fluid A Inlet, Fluid B inlet on reaction tower tower body, and wherein fluid A moves from top to bottom, stream
Body B moves from bottom to top, wherein fluid A, and fluid B is liquid or gaseous state.
At Fluid A Inlet, be provided with valve sensor A, be provided with at Fluid B inlet valve sensor B, fluid A from
On move downward, fluid B moves from bottom to top, through packing layer, reacts in packing layer.
In course of reaction, there is the conversion of speed, under normal condition, fluid keeps a kind of standard state of flow, thing
Material reaction is the most abundant, and a certain fluid is vulgar or exceeds the speed limit, and arises that cutout or turbulent flow so that react insufficient.
It is respectively provided with plug in sensor A in packing layer upper end, plug in sensor A is provided with plug-in type sensing
Device probe A, is respectively provided with plug in sensor B in packing layer upper end, is provided with plug-in type sensing on plug in sensor B
Device probe B, probe A and probe B can sense the flow velocity of mixing object.
A kind of optimal technical scheme, so that the stablizing of probe A and probe B measurement flow rate, at plug in sensor A,
It is connected to cowling panel so that measure accurately on plug in sensor B.
At work, the fluid A of valve sensor A moves downward, and the flow velocity in probe A should be valve sensor A's
Flow velocity low, concrete coefficient is the process coefficient of real reaction, as being set to a1, a1 equal to the flow velocity of probe A divided by valve
The flow velocity of door sensor A；The fluid B of valve sensor B moves upward, and the flow velocity in probe B should be than the stream of valve sensor B
Fast is low, and concrete coefficient is the process coefficient of real reaction, with the flow velocity of probe B divided by the flow velocity at valve sensor B, arranges
For b1.
Sealed by sealing ring between plug in sensor A and plug in sensor B and reaction tower, valve sensor A, valve
Door sensor B, probe A, probe B is connected with supersonic flow amount controller by data wire respectively, first, and valve sensor A, valve
Door sensor B, probe A, probe B is connected with signal processing module, the data signal gathered through processing, is then attached to surpass
Raw wave transducer, and have children outside the state plan wave transducer and filter through wave filter, it is then passed through amplifier and is amplified, and signal is passed
Being passed to oscillograph, oscillograph is connected to host computer, and host computer uses computer processor structure, and host computer enters the data gathered
Row compares calculating.Numerical value relatively and initial parameter contrast, if the change of parameter occurrence scope, host computer passes through data
Line is connected to control switch, under the effect controlling switch, controls fluid A and the speed of fluid B respectively so that reaction to
Steadily direction is run.
A kind of optimal technical scheme, is connected to printer on host computer, it is possible to data are carried out arranging printing, it is simple to thing
The analysis of material reaction.
The foregoing is only embodiments of the invention, not thereby limit the scope of the claims of the present invention, every utilize this
Equivalent structure or equivalence flow process that bright description and accompanying drawing content are made convert, or are directly or indirectly used in other relevant skills
Art field, is the most in like manner included in the scope of patent protection of the present invention.
Claims (3)
1. in a reaction tower, waste water flows through filler speed monitoring monitoring system, it is characterised in that including: reaction tower, in reaction
It is provided with packing layer in tower, on reaction tower tower body, is wherein provided with Fluid A Inlet, Fluid B inlet, sets at Fluid A Inlet
Put valve sensor A, at Fluid B inlet, be provided with valve sensor B, be respectively provided with plug-in type in packing layer upper end and pass
Sensor A, is provided with plug in sensor probe A on plug in sensor A, is respectively provided with plug-in type in packing layer upper end and passes
Sensor B, is provided with plug in sensor probe B, probe A and probe B on plug in sensor B and can sense mixing object
Flow velocity, the fluid A of valve sensor A moves downward, and the flow velocity in probe A should low, specifically at the flow velocity of valve sensor A
Coefficient be the process coefficient of real reaction be a1, a1 equal to the flow velocity of probe A divided by the flow velocity at valve sensor A, valve
The fluid B of sensor B moves upward, probe B flow velocity should flow velocity than valve sensor B low, concrete coefficient is real
The process coefficient of border reaction, with the flow velocity of probe B divided by the flow velocity at valve sensor B, is set to b1, plug in sensor A
And sealed by sealing ring between plug in sensor B and reaction tower, valve sensor A, valve sensor B, probe A, probe B
It is connected with supersonic flow amount controller by data wire respectively, valve sensor A, valve sensor B, probe A, probe B and letter
Number processing module connects, and the data signal gathered through processing, is then attached to have children outside the state plan wave transducer, and has children outside the state plan ripple transducing
Device filters through wave filter, is then passed through amplifier and is amplified, and signal is transferred to oscillograph, and oscillograph is connected to
Position machine, host computer uses computer processor structure, and host computer compares calculating the data gathered, and the numerical value compared is with just
The parameter begun contrasts, if the change of parameter occurrence scope, host computer is connected to control switch by data wire, opens in control
Under the effect closed, control fluid A and the speed of fluid B respectively so that reaction runs to steady direction.
In a kind of reaction tower the most according to claim 1, waste water flows through filler speed monitoring monitoring system, it is characterised in that
So that stablizing of probe A and probe B measurement flow rate, plug in sensor A, plug in sensor B are connected to rectification
Plate.
In a kind of reaction tower the most according to claim 1, waste water flows through filler speed monitoring monitoring system, it is characterised in that
Host computer is connected to printer, it is possible to data are carried out arranging printing, it is simple to the analysis of material reaction.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610442747.1A CN106123981B (en) | 2016-06-20 | 2016-06-20 | Waste water flows through filler speed monitoring monitoring system in a kind of reaction tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610442747.1A CN106123981B (en) | 2016-06-20 | 2016-06-20 | Waste water flows through filler speed monitoring monitoring system in a kind of reaction tower |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106123981A true CN106123981A (en) | 2016-11-16 |
| CN106123981B CN106123981B (en) | 2019-04-02 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610442747.1A Expired - Fee Related CN106123981B (en) | 2016-06-20 | 2016-06-20 | Waste water flows through filler speed monitoring monitoring system in a kind of reaction tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106123981B (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002113323A (en) * | 2000-10-05 | 2002-04-16 | Seiichi Futaboshi | Deodorizing equipment |
| US20090035197A1 (en) * | 2005-01-31 | 2009-02-05 | Hovis Keith W | Alkylation Process with Recontacting in Settler |
| CN101549255A (en) * | 2009-05-05 | 2009-10-07 | 浙江省环境保护科学设计研究院 | Method for treating organic exhaust-gas generated in waste plastic granulation process |
| CN101735860A (en) * | 2008-11-21 | 2010-06-16 | 沈阳瑞格电器制冷设备有限公司 | Raw gas purifying and emulsifying tower |
| CN202705140U (en) * | 2011-12-15 | 2013-01-30 | 上海熊猫机械(集团)有限公司 | Energy-saving sewage treating equipment |
-
2016
- 2016-06-20 CN CN201610442747.1A patent/CN106123981B/en not_active Expired - Fee Related
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002113323A (en) * | 2000-10-05 | 2002-04-16 | Seiichi Futaboshi | Deodorizing equipment |
| US20090035197A1 (en) * | 2005-01-31 | 2009-02-05 | Hovis Keith W | Alkylation Process with Recontacting in Settler |
| CN101735860A (en) * | 2008-11-21 | 2010-06-16 | 沈阳瑞格电器制冷设备有限公司 | Raw gas purifying and emulsifying tower |
| CN101549255A (en) * | 2009-05-05 | 2009-10-07 | 浙江省环境保护科学设计研究院 | Method for treating organic exhaust-gas generated in waste plastic granulation process |
| CN202705140U (en) * | 2011-12-15 | 2013-01-30 | 上海熊猫机械(集团)有限公司 | Energy-saving sewage treating equipment |
Non-Patent Citations (1)
| Title |
|---|
| 杨启明，饶霁阳: "《石油化工过程设备设计》", 30 November 2012, 石油工业出版社 * |
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| Publication number | Publication date |
|---|---|
| CN106123981B (en) | 2019-04-02 |
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Granted publication date: 20190402 |
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