CN108479646A - A kind of pneumatic mixing arrangement of spent acid reduction - Google Patents
A kind of pneumatic mixing arrangement of spent acid reduction Download PDFInfo
- Publication number
- CN108479646A CN108479646A CN201810297213.3A CN201810297213A CN108479646A CN 108479646 A CN108479646 A CN 108479646A CN 201810297213 A CN201810297213 A CN 201810297213A CN 108479646 A CN108479646 A CN 108479646A
- Authority
- CN
- China
- Prior art keywords
- spent acid
- iron powder
- air
- reaction tank
- mixing tube
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
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- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/1818—Feeding of the fluidising gas
-
- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/005—Separating solid material from the gas/liquid stream
- B01J8/007—Separating solid material from the gas/liquid stream by sedimentation
-
- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
- B01J8/22—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid
Abstract
The invention belongs to dangerous waste processing technology fields, and in particular to a kind of pneumatic mixing arrangement of spent acid reduction, agent structure include：Air compressor, air pipeline, mixing tube, baffle, inclined plate, iron powder, feed inlet, outlet valve and reaction tank；It is provided with inclined plate at the bottom surrounding of reaction tank, the bottom of pond of reaction tank is loaded with to restore the iron powder of spent acid, iron powder concentrates the middle for being deposited in reaction tank under the guiding of inclined plate inclined surface, the centre of reaction tank is arranged above the mixing tube placed vertically, the air that air compressor generates is delivered to the bottom of reaction tank by air pipeline, spent acid is blown afloat, spent acid drives iron powder to enter mixing tube, iron powder and spent acid are in mixing tube in uphill process, it is acute and be sufficiently mixed reaction under airflow stirring effect, its agent structure is simple, design concept is ingenious, it is safe and convenient to use, application environment is friendly, wide market.
Description
Technical field:
The invention belongs to dangerous waste processing technology fields, and in particular to a kind of pneumatic mixing arrangement of spent acid reduction passes through air
Compressor come to reduction pond in conveying air come drive bottom of pond iron powder flow fully to be contacted with spent acid and carry out reduction reaction.
Background technology:
With the continuous propulsion of process of industrialization, the spent acid generated in chemical industry is more and more, these spent acid or generation
In processes such as the nitrification of organic matter, esterification, sulfonation, alkylation, catalysis and gas dries, or result from titanium white production, steel
During pickling and gas dry etc., these spent acid contain certain density heavy metal contaminants, and work is purified in spent acid heavy metal
In skill, iron powder reducing method is the heavy metal purification process technique of generally use, and the mechanism of heavy metal purification is iron powder and spent acid
In heavy metal ion occur redox reaction, by heavy metal precipitation or filtering remove.In Practical Project, iron powder and spent acid
Be sufficiently mixed contact, determine the efficiency of redox reaction and the utilization rate of iron powder, but iron powder proportion is larger, is easy the bottom of at
Portion corner deposits, it is difficult to be stirred fully, for these reasons, by iron powder reducing spent acid, there are still anti-in the prior art
The defect that efficiency is low, the reaction time is long, iron powder consumption is big is answered, the processing cost of spent acid is caused also to remain high.Therefore, this hair
Bright design prepares a kind of pneumatic mixing arrangement of spent acid reduction, and that improves iron powder and spent acid by making iron powder constantly float reacts effect
Rate, using effect are good.
Invention content：
It is an object of the invention to overcome disadvantage of the existing technology, seek to design it is a kind of can be abundant with spent acid by iron powder
Mixed process unit is solved corner deposition problems, is realized well-mixed effect using the method pneumatically mixed.
To achieve the goals above, the agent structure that spent acid of the present invention restores pneumatic mixing arrangement includes：This hair
The agent structure that the bright spent acid being related to restores pneumatic mixing arrangement includes：Air compressor, air pipeline, mixing tube, baffle, tiltedly
Plate, iron powder, feed inlet, outlet valve and reaction tank；It is provided with inclined plate at the bottom surrounding of reaction tank, to make the pond of reaction tank
Bottom forms inverted cone-shaped structure, and the bottom of pond of reaction tank is loaded with to restore the iron powder of spent acid, guiding of the iron powder in inclined plate inclined surface
Lower to concentrate the middle for being deposited in reaction tank, the centre of reaction tank is arranged above the mixing tube placed vertically, to convey
One end of the air pipeline of air extends to the bottom end of mixing tube, and the other end is connect with air compressor, and air compressor generates
Air the bottom of reaction tank is delivered to by air pipeline, spent acid is blown afloat, spent acid drives iron powder to enter mixing tube, iron powder with
Spent acid is acute under airflow stirring effect and be sufficiently mixed reaction in mixing tube in uphill process；Mixing tube is arranged above
The baffle for having upper and lower bottomless cylindrical, after mixed liquor enters baffle, while baffle can make air smoothly escape liquid level, also
Spent acid can be made to be folded to downlink, iron powder free sedimentation, without making spent acid stream that iron powder be driven to be discharged by outlet valve, precipitation
Iron powder is collected to mixing bottom of the tube through inclined plate again；The top place in left side of reaction tank is provided with to convey the feed inlet of spent acid, instead
The top place in right side of Ying Chi is provided with that the outlet valve for having restored spent acid is discharged.
Further, the internal diameter of baffle of the present invention is more than the internal diameter of mixing tube, in order to the spent acid after restoring
It outflow and flows downward along the inner cavity of baffle is smooth out of mixing tube.
Further, within feed inlet of the present invention is higher 5cm than outlet valve vertical height, in order to which liquid level can be automatic
Form balance.
Further, air pipeline caliber of the present invention is less than mixing tube, and air pipeline caliber is at most no more than mixing
The 1/2 of pipe caliber can be convenient for air that can fully enter mixing tube in the size range, and can realize that air water is fully mixed
It closes.
Further, air pipeline of the present invention extends to one end of mixing infratubal port and the lower port of mixing tube is held
It is flat, or higher than mixing within infratubal port 5cm, when ensuring that the air of air pipeline is all blown into mixing tube, can be formed
Enough jet streams make iron powder, abrasive grit fully suck mixing tube, while upward because of air pipeline nozzle, can also prevent equipment from stopping
When only running, the iron powder on inclined plate piles up air pipeline nozzle, causes to block.
In the use of the present invention, first pouring into iron powder in reaction tank, it is then turned on feed inlet and spent acid is delivered to reaction tank
It is interior, it opens air compressor and air is conveyed to mixing bottom of the tube by air pipeline, to drive iron powder to rise, while driving spent acid
It seethes so that reduction reaction fully occurs with iron powder, reacts the spent acid finished and is reached under the drive of air and mix nozzle upper end and go forward side by side
Enter baffle, air escapes liquid level, and spent acid is folded to downlink, and the iron powder of iron powder free sedimentation, precipitation is collected to mixing tube again through inclined plate
Bottom, iron powder and spent acid are formed inside and outside mixing tube and are circulated, and purified spent acid is discharged through outlet valve.
Compared with prior art, the present invention what is obtained has the beneficial effect that：It can make to own by the inclined plate being obliquely installed
Iron powder concentrates on the bottom middle of reaction tank, and can be filled by coordinating with the air pipeline being arranged right over reaction tank
Point all iron powders are blown afloat, iron powder is made fully to rise floating in reaction tank, improved iron powder and the time of contact of spent acid and contact
Area greatly improves the reduction efficiency of spent acid, saves reduction cost；Iron powder after simultaneous reactions can pass through after falling
The guiding of inclined plate is gathered in reaction tank bottom middle automatically, then proceedes to cycle and floats and carry out reduction reaction, improves anti-
Efficiency is answered, ensure that the abundant progress of redox reaction；Baffle can effectively change the iron powder being discharged by mixing tube and give up
The flow direction of acid, makes iron powder deposit downwards, to prevent it from being taken out of from outlet valve by spent acid, agent structure is simple, design concept
Ingenious, safe and convenient to use, application environment is friendly, wide market.
Description of the drawings：
Fig. 1 is the agent structure principle schematic of the present invention.
Specific implementation mode：
The invention will be further described by way of example and in conjunction with the accompanying drawings.
Embodiment 1：
The agent structure that the spent acid that the present embodiment is related to restores pneumatic mixing arrangement includes：Air compressor 1, air pipeline
2, mixing tube 3, baffle 4, inclined plate 5, iron powder 6, feed inlet 7, outlet valve 8 and reaction tank 9；It is set at the bottom surrounding of reaction tank 9
It is equipped with inclined plate 5, to make the bottom of pond of reaction tank 9 form inverted cone-shaped structure, the bottom of pond of reaction tank 9 is loaded with to restore spent acid
Iron powder 6, iron powder 6 concentrate the middle for being deposited in reaction tank 9 under the guiding of 5 inclined surface of inclined plate, the centre of reaction tank 9 just on
Side is provided with the mixing tube 3 placed vertically, to convey the bottom end that one end of air pipeline 2 of air extends to mixing tube 3, separately
One end is connect with air compressor 1, and the air that air compressor 1 generates is delivered to the bottom of reaction tank 9 by air pipeline 2,
Spent acid is blown afloat, spent acid drives iron powder 6 to enter mixing tube 3, and iron powder 6 in uphill process, is stirred with spent acid in mixing tube 3 in air-flow
The effect of mixing is lower acute and is sufficiently mixed reaction；The baffle 4 for being arranged above upper and lower bottomless cylindrical of mixing tube 3, mixed liquor
Into after baffle 4, while baffle 4 can make air smoothly escape liquid level, additionally it is possible to spent acid be made to be folded to downlink, iron powder 6 freely
Precipitation, without making spent acid stream that iron powder 6 be driven to be discharged by outlet valve 8, the iron powder 6 of precipitation is collected to mixing again through inclined plate 5
3 bottom of pipe；The top place in left side of reaction tank 9 is provided with to convey the feed inlet 7 of spent acid, and the top place in right side of reaction tank 9 is set
It is equipped with that the outlet valve 8 for having restored spent acid is discharged.
Further, the internal diameter of the baffle 4 described in the present embodiment is more than the internal diameter of mixing tube 3, after in order to restore
Spent acid outflow and flows downward along the inner cavity of baffle 4 is smooth out of mixing tube 3.
Further, within feed inlet 7 described in the present embodiment is higher 5cm than 8 vertical height of outlet valve, in order to liquid level
Balance can be automatically formed.
Further, 2 caliber of air pipeline described in the present embodiment is less than mixing tube 3, and 2 caliber of air pipeline is at most no more than
The 1/2 of 3 caliber of mixing tube can be convenient for air that can fully enter mixing tube 3, and can realize that air water fills in the size range
Divide mixing.
Further, air pipeline 2 described in the present embodiment extends under one end and the mixing tube 3 of 3 lower port of mixing tube
Port maintains an equal level, or is higher than within 3 lower port 5cm of mixing tube, when ensuring that the air of air pipeline 2 is all blown into mixing tube 3,
Enough jet streams can be formed, so that iron powder, abrasive grit is fully sucked mixing tube, while upward because of 2 nozzle of air pipeline, can also prevent
When only equipment is out of service, the iron powder on inclined plate piles up 2 nozzle of air pipeline, causes to block.
When the present embodiment is in use, first iron powder 6 is poured into reaction tank 9, is then turned on feed inlet 7 and is delivered to spent acid instead
It answers in pond 9, opens air compressor 1 and air is conveyed to 3 bottom of mixing tube by air pipeline 2, to drive iron powder 6 to rise, together
When drive spent acid seethe with fully with iron powder 6 occur reduction reaction, react the spent acid finished and reach mixing under the drive of air
3 mouthfuls of upper ends of pipe simultaneously enter baffle 4, and air escapes liquid level, and spent acid is folded to downlink, and 6 free sedimentation of iron powder, the iron powder 6 of precipitation is through oblique
Plate 5 is collected to 3 bottom of mixing tube, iron powder 6 and spent acid and is circulated in inside and outside formed of mixing tube 3 again, and purified spent acid is through going out
Mouth valve 8 is discharged.
Claims (6)
1. a kind of spent acid restores pneumatic mixing arrangement, it is characterised in that its agent structure includes：Spent acid reduction of the present invention
Pneumatically the agent structure of mixing arrangement includes：Air compressor, air pipeline, mixing tube, baffle, inclined plate, iron powder, feed inlet,
Outlet valve and reaction tank；It is provided with inclined plate at the bottom surrounding of reaction tank, to make the bottom of pond of reaction tank form back taper knot
Structure, the bottom of pond of reaction tank are loaded with to restore the iron powder of spent acid, and iron powder is concentrated under the guiding of inclined plate inclined surface to be deposited in instead
The middle of Ying Chi, the centre of reaction tank are arranged above the mixing tube placed vertically, to convey the air pipeline of air
One end extend to the bottom end of mixing tube, the other end is connect with air compressor, and the air that air compressor generates passes through air
Pipeline blows afloat spent acid to the bottom of reaction tank, and spent acid drives iron powder to enter mixing tube, and iron powder is with spent acid in mixing tube
It is acute under airflow stirring effect and be sufficiently mixed reaction in uphill process；Mixing tube is arranged above circle bottomless up and down
The baffle of tubular, after mixed liquor enters baffle, while baffle can make air smoothly escape liquid level, additionally it is possible to spent acid be made to be folded to
Downlink, iron powder free sedimentation, without making spent acid stream that iron powder be driven to be discharged by outlet valve, the iron powder of precipitation converges again through inclined plate
Collection extremely mixing bottom of the tube；The top place in left side of reaction tank is provided with to convey the feed inlet of spent acid, and the right side of reaction tank is top
Place is provided with that the outlet valve for having restored spent acid is discharged.
2. a kind of spent acid according to claim 1 restores pneumatic mixing arrangement, it is characterised in that the internal diameter of baffle is more than mixed
The internal diameter for closing pipe, with flowing out out of mixing tube in order to the spent acid after restoring and flow downward along the inner cavity of baffle is smooth.
3. a kind of spent acid according to claim 1 restores pneumatic mixing arrangement, it is characterised in that feed inlet compares outlet valve
Within the high 5cm of vertical height, in order to which liquid level can automatically form balance.
4. a kind of spent acid according to claim 1 restores pneumatic mixing arrangement, it is characterised in that air pipeline caliber is less than
Mixing tube, air pipeline caliber are at most no more than the 1/2 of mixing tube caliber, can be complete convenient for air in the size range
Portion enters mixing tube, and can realize that air water is sufficiently mixed.
5. a kind of spent acid according to claim 4 restores pneumatic mixing arrangement, it is characterised in that air pipeline extends to mixed
The lower port of one end and mixing tube for closing infratubal port maintains an equal level, or higher than mixing within infratubal port 5cm, to ensure air pipeline
Air when all blowing into mixing tube, enough jet streams can be formed, iron powder, abrasive grit is made fully to suck mixing tube, at the same because
Upward, when can also prevent equipment out of service, the iron powder on inclined plate piles up air pipeline nozzle to air pipeline nozzle, causes to block up
Plug.
6. a kind of spent acid according to any claim in claim 1-5 restores pneumatic mixing arrangement, it is characterised in that
In the use of the present invention, first pouring into iron powder in reaction tank, it is then turned on feed inlet and spent acid is delivered in reaction tank, opens empty
Air compressor conveys air by air pipeline to mixing bottom of the tube, to drive iron powder to rise, while driving spent acid to seethe to fill
Divide and reduction reaction occur with iron powder, reacts the spent acid finished and reach mixing nozzle upper end under the drive of air and enter baffle,
Air escapes liquid level, and spent acid is folded to downlink, and the iron powder of iron powder free sedimentation, precipitation is collected to mixing bottom of the tube, iron through inclined plate again
Powder and spent acid are formed inside and outside mixing tube to be circulated, and purified spent acid is discharged through outlet valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810297213.3A CN108479646A (en) | 2018-03-30 | 2018-03-30 | A kind of pneumatic mixing arrangement of spent acid reduction |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810297213.3A CN108479646A (en) | 2018-03-30 | 2018-03-30 | A kind of pneumatic mixing arrangement of spent acid reduction |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108479646A true CN108479646A (en) | 2018-09-04 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810297213.3A Pending CN108479646A (en) | 2018-03-30 | 2018-03-30 | A kind of pneumatic mixing arrangement of spent acid reduction |
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| Country | Link |
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| CN (1) | CN108479646A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113800680A (en) * | 2021-09-30 | 2021-12-17 | 维尔利环保科技集团股份有限公司 | Reactor and method for treating landfill leachate membrane concentrated solution based on reactor |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1435275A (en) * | 2002-02-01 | 2003-08-13 | 中国石油天然气股份有限公司 | Multi-stage circular flow reactor |
| CN201201913Y (en) * | 2008-03-19 | 2009-03-04 | 胡志刚 | Flocculation reaction pot |
| CN201567259U (en) * | 2009-11-19 | 2010-09-01 | 陈丰 | Device for treating sulfonated waste water |
| CN102120674A (en) * | 2011-01-25 | 2011-07-13 | 大连理工大学 | Zero-valent iron fortified anaerobic hydrolysis-acidification sewage treatment method |
| CN102795690A (en) * | 2012-08-24 | 2012-11-28 | 四川大学 | Wastewater treatment method by ultrasonic reinforcement micron-scale iron-copper bimetallic particle |
| CN103043847A (en) * | 2011-10-17 | 2013-04-17 | 中国石油天然气股份有限公司 | Floatation-biochemical treatment method and apparatus of ultra-thick oil sewage |
| CN206069472U (en) * | 2016-09-21 | 2017-04-05 | 武汉兴天宇环境股份有限公司 | A kind of hybrid micro-electrolysis reactor of air |
-
2018
- 2018-03-30 CN CN201810297213.3A patent/CN108479646A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1435275A (en) * | 2002-02-01 | 2003-08-13 | 中国石油天然气股份有限公司 | Multi-stage circular flow reactor |
| CN201201913Y (en) * | 2008-03-19 | 2009-03-04 | 胡志刚 | Flocculation reaction pot |
| CN201567259U (en) * | 2009-11-19 | 2010-09-01 | 陈丰 | Device for treating sulfonated waste water |
| CN102120674A (en) * | 2011-01-25 | 2011-07-13 | 大连理工大学 | Zero-valent iron fortified anaerobic hydrolysis-acidification sewage treatment method |
| CN103043847A (en) * | 2011-10-17 | 2013-04-17 | 中国石油天然气股份有限公司 | Floatation-biochemical treatment method and apparatus of ultra-thick oil sewage |
| CN102795690A (en) * | 2012-08-24 | 2012-11-28 | 四川大学 | Wastewater treatment method by ultrasonic reinforcement micron-scale iron-copper bimetallic particle |
| CN206069472U (en) * | 2016-09-21 | 2017-04-05 | 武汉兴天宇环境股份有限公司 | A kind of hybrid micro-electrolysis reactor of air |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113800680A (en) * | 2021-09-30 | 2021-12-17 | 维尔利环保科技集团股份有限公司 | Reactor and method for treating landfill leachate membrane concentrated solution based on reactor |
| CN113800680B (en) * | 2021-09-30 | 2023-08-25 | 维尔利环保科技集团股份有限公司 | Reactor and method for treating landfill leachate membrane concentrate based on same |
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| PB01 | Publication | ||
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| RJ01 | Rejection of invention patent application after publication | ||
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Application publication date: 20180904 |