CN202346813U - Device for removing mercury from high concentration acid - Google Patents
Device for removing mercury from high concentration acid Download PDFInfo
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- CN202346813U CN202346813U CN2011204780413U CN201120478041U CN202346813U CN 202346813 U CN202346813 U CN 202346813U CN 2011204780413 U CN2011204780413 U CN 2011204780413U CN 201120478041 U CN201120478041 U CN 201120478041U CN 202346813 U CN202346813 U CN 202346813U
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- mercury
- acid
- ejector
- hydrogen sulfide
- reactor drum
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Abstract
The utility model discloses a device for removing mercury from high concentration acid. The device comprises a sealed reactor for storing acid, a circulating pump, a jet device provided with a liquid inlet, a gas inlet and a diffusion tube, and a sealed hydrogen sulfide storage tank; the bottom of the reactor is connected with the circulating pump through a pipeline; the circulating pump is connected to the liquid inlet of the jet device through a pipeline; the jet device is arranged on the upper part of the reactor; the diffusion tube of the jet device is communicated with the reactor; and the hydrogen sulfide storage tank is connected with the gas inlet of the jet device and the upper part of the reactor through a pipeline respectively. The mercury concentration in the acid treated by the device is less than 0.05mg/L, and the quality of the acid cannot be influenced in the treatment process.
Description
Technical field
The utility model relates to the device that removes mercury in a kind of high concentrated acid, belongs to the chemical industry environmental protection field.
Background technology
Mercury is important heavy metal element, claims mercury again, is a kind of silvery white, the liquid metal of unique one-tenth under the normal temperature.It is raw material with mercury that the industry of kind more than 80 is arranged according to statistics in the world, and the purposes of mercury then reaches kind more than 3000.Enter mercury and compound thereof in the water body, form the mercury of various forms, even can change into the very big methyl compounds of toxicity through physics, chemistry and biological action.The minamata disease that nineteen fifty-three occurs in Japan is caused by the Monomethyl mercury chloride polluted waters of chemical plant emission.Mainly contain chemical precipitation method, metallic reducing method, active carbon adsorption, ion exchange method, electrolytic process, microbial method etc. to its traditional treatment process of mercury-containing waste water.
Chemical precipitation method is to use more general a kind of mercury treatment process, can handle different concns, different types of mercury salt, and method commonly used has two kinds of coagulant sedimentation and sulphide precipitations.
Its principle of coagulant sedimentation is in mercury-containing waste water, to add coagulating agent (lime, molysite, aluminium salt), is under 8～10 the weak basic condition at pH, forms the oxyhydroxide flocs unit, and mercury is had throwing out, and the mercury co-precipitation is separated out.Sulphide precipitation utilizes Na under the weak basic condition
2S, the S among the MgS
2-With Hg
+/ Hg
2+Between stronger avidity is arranged, generate the minimum zunsober deposition of solubility and from solution, remove.
Electrolytic process is to utilize the electrochemical properties of metal, and under effect of DC, mercury compound is dissociated into mercury ion at anode, becomes MERCURY METAL 99.99(500+500FLASKS) in cathodic reduction, and removes the mercury in the waste water.But this method shortcoming is the ion concentration of mercury in the water can not fall very lowly.So electrolytic process is not suitable for handles the mercury ion waste water that contains lower concentration, and this kind method power consumption is big, cost of investment is high, is easy to generate mercuryvapour, forms secondary pollution.
Ion exchange method is compared with electrolytic process with the precipitator method, and it can remove the mercury ion of lower concentration from solution.Ion exchange method is carried out in ion-exchanger, and (SH) ion exchange resin absorption mercury ion reaches the purpose of removing mercury ion in the water with the macropore sulfydryl.This process is a reversible, and ion exchange resin can be regenerated, and generally is used for second-stage treatment.The wash-out of resin is with the concentrated hydrochloric acid of 40 times of resin volumes, eluting rate 90%.But this method receives the influence of impurity in the waste water and the restriction of exchanger kind, output and cost.
The absorption method removal of mercury mainly contains, active carbon adsorption, chitin absorption method, zeolite molecular sieve absorption method, modified alta-mud absorption method, flyash absorption method, corn cob meal absorption method and rice husk ash absorption method.Rice shell, bagasse, soybean peel, sawdust, Exocarpium cocois (Cocos nucifera L), Pericarppium arachidis hypogaeae, apple core and flying dust after the modification can both be used as sorbent treatment mercury.Gac has great surface-area, in reactivation process, form some oxygen-containing functional groups (COOH ,-OH ,-C=O) make gac have chemisorption and catalyzed oxidation, reductive performance, can effectively remove heavy metal.With the higher waste water of activated carbon treatment mercury content, can obtain very high clearance (85%～99%).Handle the lower waste water of mercury content,, can obtain the very low water outlet of mercury content though clearance is not high enough.
The wool absorption process is that to utilize wool be a kind of protein; Constitute in the proteinic amino acid and contain Gelucystine; It combines to make wool molecule crosslinked with disulphide, but this combination can be passed through reduction reaction, and the effects such as water decomposition, enzyme that add are cut off into sulfydryl; And heavy metals such as mercury are easy and the sulfydryl reaction, and the modified wool of therefore holding sulfydryl can trap heavy metals.Modified wool has good trapping ability to Trace Mercury, must work out the woolen post-treating method that has adsorbed mercury at present.
Reduction method is theoretical according to electropotential, utilizes little and the metal (bits or powder) that electropotential is low of toxicity such as copper, zinc, aluminium, magnesium, manganese from waste water displace mercury ion, and is wherein better with iron, zinc effect.For example in the iron reduction method, pH is better at 7～8 o'clock treatment effects, and approximately 40kg industry iron powder can be removed 1kg mercury.The metallic reducing method is applicable to handles the single mercury-containing waste water of composition, and its speed of reaction is higher, can directly reclaim MERCURY METAL 99.99(500+500FLASKS), but demercuration is incomplete, and need and additive method are used in combination.
Solvent extration uses the Trace Mercury in the SX waste water, and the xylene solution with containing tri-iso-octylamine extracts HgCl42-with the form of complex compound, in the aqueous solution, strip then.This method can only be used for a spot of mercury-containing waste water.
Microbial method is compared with traditional physico-chemical process, and it has the following advantages: working cost is low, needs the chemistry or the biological sludge amount of processing few; The waste liquid efficient of removing the extremely low concentration heavy metal ion is high; Operation pH and TR wide (pH3～9,4～90 ℃ of temperature); High adsorption rate, highly selective.And it is effective especially when being the waste water of 1～100mg/L that microbial method is handled the mercury mass concentration.Microbial method has remedied the deficiency that existing technology can not be reduced to mercury ion massfraction in the sewage 10-9 level, and it will receive increasing attention with its novelty, special advantages.
The object of aforesaid method main processing is mercurous heavy metal wastewater thereby; Or low acidity mercury-containing waste water; But up to the acid more than 30%, and treating processes can not influence the quality of handling back acid for massfraction, and above-mentioned ordinary method all can't realize; And applicant of the present invention has researched and developed a kind of method of handling mercurous high concentrated acid that is applicable to
The reactor drum top of the first step, sealing is provided with ejector; Acid in the reactor drum is passed through recycle pump by fluid inlet input jet device; The negative pressure that simultaneously swiftly flowing acid produces makes the inlet mouth of hydrogen sulfide by hydrogen sulfide storage tank entering ejector, acid and hydrogen sulfide hybrid reaction in ejector;
Hydrogen sulfide and the acid completely of second step, the zunsober that is produced after the hybrid reaction and unreacted gets in the reactor drum through the diffuser tube of ejector; Zunsober precipitates because of being insoluble to acid; The hydrogen sulfide that is insoluble to acid rises and returns the hydrogen sulfide storage tank through the output channel that is arranged at reactor drum top and recycles, and acid gets into ejector once more through recycle pump and continues to handle.
Therefore, develop a cover and be applicable to that the corollary apparatus of aforesaid method also is highly significant.
The utility model content
The purpose of the utility model provides the device of demercuration in a kind of high concentrated acid.
The device of demercuration in the high concentrated acid of the utility model comprises the hydrogen sulfide storage tank of reactor drum, recycle pump, ejector and the sealing of the sealing that is used for stock acid, and described ejector is provided with fluid inlet, inlet mouth and diffuser tube; Pipe connection is passed through to recycle pump in the bottom of described reactor drum; Recycle pump passes through the fluid inlet of pipe connection to ejector again; Described ejector is arranged at reactor drum top; The diffuser tube of ejector is communicated in the reactor drum, and described hydrogen sulfide storage tank is respectively through the inlet mouth of pipe connection ejector and the top of reactor drum.
The utlity model has following advantage:
Do not see the relevant report of technology of demercuration in high density (content is more than the 30%) acid and device at present.
This apparatus structure is simple, can realize that mercury in the acid efficiently removes with the form of zunsober, and reaction process can not be introduced new impurity and influence the quality of acid, can reclaim mercury wherein after the zunsober deposition is collected.
Description of drawings
Fig. 1 is the ejector structure diagram
Wherein: 1 is ejector, and 2 is fluid inlet, and 3 is inlet mouth, and 4 is mixing chamber, and 5 is trunnion, and 6 is diffuser tube;
Fig. 2 is a high concentrated acid demercuration reacting jet device synoptic diagram;
Wherein: 7 is reactor drum, and 8 is the hydrogen sulfide storage tank, and 9 is recycle pump, and 10 is mercurous high concentrated acid, and 11 is hydrogen sulfide.
Embodiment
Be intended to further specify the utility model below in conjunction with embodiment, and unrestricted the utility model.
The device of demercuration in the high concentrated acid of the utility model comprises reactor drum 7, recycle pump 9, the ejector 1 of the sealing that is used for stock acid and the hydrogen sulfide storage tank 8 that seals, and described ejector 1 is provided with fluid inlet 2, inlet mouth 3 and diffuser tube 6; The bottom of described reactor drum 7 is through pipe connection to recycle pump 9; Recycle pump 9 passes through the fluid inlet 2 of pipe connection to ejector 1 again; Described ejector 1 is arranged at reactor drum 7 tops; The diffuser tube 6 of ejector 1 is communicated in the reactor drum 7, and described hydrogen sulfide storage tank 8 is respectively through the inlet mouth 3 of pipe connection ejector 1 and the top of reactor drum 7.
The detailed process of the high concentrated acid that the utility model apparatus processes is mercurous is following:
Mercurous high concentrated acid gets into ejector 1 with high speed by fluid inlet 2 through recycle pump 9 in the reactor drum 7 of sealing; When mixing chamber 4 is passed through in swiftly flowing acid, can form negative pressure at mixing chamber 4, and then suck a large amount of hydrogen sulfide by inlet mouth 3; After hydrogen sulfide gets into mixing chamber 4; Generate zunsober at trunnion 5 places and the violent hybrid reaction of mercurous high concentrated acid, simultaneously with unreacted hydrogen sulfide and acid solution mixtinite completely, by diffuser tube 6 discharges; Hydrogen sulfide rises with trickle bubble in acid; Trickle bubble in uphill process with acid in mercury continue reaction and generate zunsober, zunsober is insoluble to acid and precipitates, and reaches the purpose of processing.In whole process, form material transfer efficiently.Because hydrogen sulfide storage tank 8 passes through pipe connection with reactor drum 7 upper spaces; Unreacted hydrogen sulfide is insoluble to acid and rises and return hydrogen sulfide storage tank 8 through the output channel that is arranged at reactor drum 7 tops and recycle, and acid gets into ejector 1 once more through recycle pump 9 and continues to handle.Because hydrogen sulfide mixed gas sealing and circulating between reactor drum 7 and hydrogen sulfide storage tank 8 can not produce pollution.Hydrogen sulfide can adopt sodium sulphite or Iron sulfuret and sulfur waste acid or abraum salt acid preparation, or is directly provided by system gas company.
The abraum salt acid 500ml that embodiment 1 gets certain chemical plant generation goes into reactor drum, and concentration of hydrochloric acid 31%, mercury content 21mg/L, hydrogen sulfide add into reaction with amount S: Hg=5 and wherein pass through ejector circulation 60min, remaining mercury concentration 0.042mg/L.
The abraum salt acid 500ml that embodiment 2 gets certain chemical plant generation goes into reactor drum, and concentration of hydrochloric acid 31%, mercury content 21mg/L, hydrogen sulfide add into reaction with amount S: Hg=10 and wherein pass through ejector circulation 45min, remaining mercury concentration 0.036mg/L.
The abraum salt acid 500ml that embodiment 3 gets certain chemical plant generation goes into reactor drum, concentration of hydrochloric acid 31%, mercury content 21mg/L; Hydrogen sulfide adds into reaction wherein through the ejector circulation with amount S: Hg=20; Circulation pump speed 250mL/min, cycling time 30min, remaining mercury concentration 0.028mg/L.
The abraum salt acid 500ml that embodiment 4 gets certain chemical plant generation goes into reactor drum, concentration of hydrochloric acid 31%, mercury content 21mg/L; Hydrogen sulfide adds into reaction wherein through the ejector circulation with amount S: Hg=30; Circulation pump speed 250mL/min, cycling time 20min, remaining mercury concentration 0.031mg/L.
Claims (1)
1. the device of demercuration in the high concentrated acid is characterized in that comprise the hydrogen sulfide storage tank of reactor drum, recycle pump, ejector and the sealing of the sealing that is used for stock acid, described ejector is provided with fluid inlet, inlet mouth and diffuser tube; Pipe connection is passed through to recycle pump in the bottom of described reactor drum; Recycle pump passes through the fluid inlet of pipe connection to ejector again; Described ejector is arranged at reactor drum top; The diffuser tube of ejector is communicated in the reactor drum, and described hydrogen sulfide storage tank is respectively through the inlet mouth of pipe connection ejector and the top of reactor drum.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204780413U CN202346813U (en) | 2011-11-25 | 2011-11-25 | Device for removing mercury from high concentration acid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204780413U CN202346813U (en) | 2011-11-25 | 2011-11-25 | Device for removing mercury from high concentration acid |
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| Publication Number | Publication Date |
|---|---|
| CN202346813U true CN202346813U (en) | 2012-07-25 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011204780413U Expired - Lifetime CN202346813U (en) | 2011-11-25 | 2011-11-25 | Device for removing mercury from high concentration acid |
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| CN (1) | CN202346813U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102491477A (en) * | 2011-11-25 | 2012-06-13 | 中南大学 | Method and device for removing mercury from high concentration acid |
| CN106746010A (en) * | 2016-12-30 | 2017-05-31 | 四川师范大学 | The processing method of chromate waste water |
-
2011
- 2011-11-25 CN CN2011204780413U patent/CN202346813U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102491477A (en) * | 2011-11-25 | 2012-06-13 | 中南大学 | Method and device for removing mercury from high concentration acid |
| CN106746010A (en) * | 2016-12-30 | 2017-05-31 | 四川师范大学 | The processing method of chromate waste water |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20120725 |
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| CX01 | Expiry of patent term |