CN114733897A - In-situ catalytic oxidation inactivation method for iron-sulfur oxidation acid-producing bacteria in extremely-acidified pyrite mountain soil - Google Patents
In-situ catalytic oxidation inactivation method for iron-sulfur oxidation acid-producing bacteria in extremely-acidified pyrite mountain soil Download PDFInfo
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- 239000002689 soil Substances 0.000 title claims abstract description 80
- 229910052683 pyrite Inorganic materials 0.000 title claims abstract description 54
- NIFIFKQPDTWWGU-UHFFFAOYSA-N pyrite Chemical compound [Fe+2].[S-][S-] NIFIFKQPDTWWGU-UHFFFAOYSA-N 0.000 title claims abstract description 54
- 239000011028 pyrite Substances 0.000 title claims abstract description 53
- 230000003647 oxidation Effects 0.000 title claims abstract description 49
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 49
- 238000000034 method Methods 0.000 title claims abstract description 36
- 239000002253 acid Substances 0.000 title claims abstract description 34
- MBMLMWLHJBBADN-UHFFFAOYSA-N Ferrous sulfide Chemical compound [Fe]=S MBMLMWLHJBBADN-UHFFFAOYSA-N 0.000 title claims abstract description 27
- 102000005298 Iron-Sulfur Proteins Human genes 0.000 title claims abstract description 27
- 108010081409 Iron-Sulfur Proteins Proteins 0.000 title claims abstract description 27
- 230000003197 catalytic effect Effects 0.000 title claims abstract description 18
- 238000011065 in-situ storage Methods 0.000 title claims abstract description 18
- 241000894006 Bacteria Species 0.000 title claims abstract description 17
- 230000002779 inactivation Effects 0.000 title claims abstract description 17
- 230000001590 oxidative effect Effects 0.000 claims abstract description 18
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims abstract description 17
- 235000011941 Tilia x europaea Nutrition 0.000 claims abstract description 17
- 239000004571 lime Substances 0.000 claims abstract description 17
- WQYVRQLZKVEZGA-UHFFFAOYSA-N hypochlorite Chemical compound Cl[O-] WQYVRQLZKVEZGA-UHFFFAOYSA-N 0.000 claims abstract description 16
- 239000007800 oxidant agent Substances 0.000 claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 12
- 239000002344 surface layer Substances 0.000 claims abstract description 6
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 32
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 12
- 239000011593 sulfur Substances 0.000 claims description 11
- 229910052717 sulfur Inorganic materials 0.000 claims description 11
- 239000003795 chemical substances by application Substances 0.000 claims description 10
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- ZKQDCIXGCQPQNV-UHFFFAOYSA-N Calcium hypochlorite Chemical compound [Ca+2].Cl[O-].Cl[O-] ZKQDCIXGCQPQNV-UHFFFAOYSA-N 0.000 claims description 3
- 229920000388 Polyphosphate Polymers 0.000 claims description 3
- 239000004115 Sodium Silicate Substances 0.000 claims description 3
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- 239000001205 polyphosphate Substances 0.000 claims description 3
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- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 claims description 3
- 229910052911 sodium silicate Inorganic materials 0.000 claims description 3
- 239000000454 talc Substances 0.000 claims description 3
- 229910052623 talc Inorganic materials 0.000 claims description 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 2
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 claims description 2
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 claims description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims description 2
- 239000005708 Sodium hypochlorite Substances 0.000 claims description 2
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims description 2
- 229910052802 copper Inorganic materials 0.000 claims description 2
- 239000010949 copper Substances 0.000 claims description 2
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- 239000011574 phosphorus Substances 0.000 claims description 2
- 229910052698 phosphorus Inorganic materials 0.000 claims description 2
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 claims description 2
- 239000011701 zinc Substances 0.000 claims description 2
- 229910052725 zinc Inorganic materials 0.000 claims description 2
- 239000002131 composite material Substances 0.000 claims 1
- 239000003814 drug Substances 0.000 claims 1
- 244000005700 microbiome Species 0.000 abstract description 29
- 230000020477 pH reduction Effects 0.000 abstract description 13
- 150000001875 compounds Chemical class 0.000 abstract description 9
- 230000002378 acidificating effect Effects 0.000 abstract description 7
- 239000010410 layer Substances 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract description 4
- 238000006555 catalytic reaction Methods 0.000 abstract description 3
- 230000002401 inhibitory effect Effects 0.000 abstract description 3
- 238000005056 compaction Methods 0.000 abstract description 2
- 208000021302 gastroesophageal reflux disease Diseases 0.000 description 8
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- 230000009471 action Effects 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 4
- QWPPOHNGKGFGJK-UHFFFAOYSA-N hypochlorous acid Chemical compound ClO QWPPOHNGKGFGJK-UHFFFAOYSA-N 0.000 description 4
- 238000002955 isolation Methods 0.000 description 4
- 230000007246 mechanism Effects 0.000 description 4
- NFMAZVUSKIJEIH-UHFFFAOYSA-N bis(sulfanylidene)iron Chemical compound S=[Fe]=S NFMAZVUSKIJEIH-UHFFFAOYSA-N 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 230000012010 growth Effects 0.000 description 3
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- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
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- 230000031018 biological processes and functions Effects 0.000 description 2
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- 241000028926 Acidibacillus ferrooxidans Species 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 241000495426 Thiobacter Species 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- MJLGNAGLHAQFHV-UHFFFAOYSA-N arsenopyrite Chemical compound [S-2].[Fe+3].[As-] MJLGNAGLHAQFHV-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004177 carbon cycle Methods 0.000 description 1
- 229910052951 chalcopyrite Inorganic materials 0.000 description 1
- DVRDHUBQLOKMHZ-UHFFFAOYSA-N chalcopyrite Chemical compound [S-2].[S-2].[Fe+2].[Cu+2] DVRDHUBQLOKMHZ-UHFFFAOYSA-N 0.000 description 1
- 238000001311 chemical methods and process Methods 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- BUGICWZUDIWQRQ-UHFFFAOYSA-N copper iron sulfane Chemical compound S.[Fe].[Cu] BUGICWZUDIWQRQ-UHFFFAOYSA-N 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 210000003608 fece Anatomy 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- SZVJSHCCFOBDDC-UHFFFAOYSA-N iron(II,III) oxide Inorganic materials O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- JQJCSZOEVBFDKO-UHFFFAOYSA-N lead zinc Chemical compound [Zn].[Pb] JQJCSZOEVBFDKO-UHFFFAOYSA-N 0.000 description 1
- XCAUINMIESBTBL-UHFFFAOYSA-N lead(ii) sulfide Chemical compound [Pb]=S XCAUINMIESBTBL-UHFFFAOYSA-N 0.000 description 1
- 239000010871 livestock manure Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 229910052960 marcasite Inorganic materials 0.000 description 1
- 230000010534 mechanism of action Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
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- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
- 239000003642 reactive oxygen metabolite Substances 0.000 description 1
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- WGPCGCOKHWGKJJ-UHFFFAOYSA-N sulfanylidenezinc Chemical compound [Zn]=S WGPCGCOKHWGKJJ-UHFFFAOYSA-N 0.000 description 1
- 229910052569 sulfide mineral Inorganic materials 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09C—RECLAMATION OF CONTAMINATED SOIL
- B09C1/00—Reclamation of contaminated soil
- B09C1/08—Reclamation of contaminated soil chemically
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09C—RECLAMATION OF CONTAMINATED SOIL
- B09C2101/00—In situ
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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- Life Sciences & Earth Sciences (AREA)
- Soil Sciences (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
本发明具体涉及一种极酸化硫铁矿山土壤中铁硫氧化产酸菌的原位催化氧化灭活方法,对极酸化硫铁矿山土壤进行表面修整,复配氧化药剂,向修整后的矿山土壤0~0.5m深度的土壤中施入复配的氧化药剂并进行翻堆混合,喷洒水,养护3~7天,之后覆盖石灰以调节表层pH值。本发明利用极酸性硫铁矿山中天然存在的H+和Fe2+催化次氯酸盐产生强氧化作用,灭活铁硫氧化产酸微生物从而抑制土壤酸化,并对下层土壤形成覆盖层保护避免氧化酸化。本发明方法操作简单,原位催化作用使次氯酸盐需求量大幅减少,相比于单纯的石灰覆盖技术大幅降低石灰用量,避免土壤板结问题,投入成本低廉,抑制酸化效果好,不易返酸,可用作极酸化硫铁矿山生态修复的前处理步骤。The invention specifically relates to an in-situ catalytic oxidation inactivation method for iron-sulfur oxidation acid-producing bacteria in extremely acidified pyrite mine soil. The compound oxidizing agent is applied to the soil at a depth of 0-0.5m, and the piles are turned and mixed, sprayed with water, cured for 3-7 days, and then covered with lime to adjust the pH value of the surface layer. The invention utilizes the naturally occurring H + and Fe 2+ in the extremely acidic pyrite mine to catalyze the strong oxidation of hypochlorite, inactivate the iron-sulfur oxidative acid-producing microorganisms, thereby inhibiting soil acidification, and forms a covering layer to protect the lower soil to avoid Oxidative acidification. The method of the invention is simple to operate, the in-situ catalysis greatly reduces the demand for hypochlorite, greatly reduces the amount of lime compared with the simple lime covering technology, avoids the problem of soil compaction, has low input cost, good effect of inhibiting acidification, and is not easy to return to acid. , which can be used as a pretreatment step for the ecological restoration of extremely acidified pyrite mines.
Description
技术领域technical field
本发明属于矿山生态修复技术领域,尤其是涉及一种极酸化硫铁矿山土壤中铁硫氧化产酸菌的原位催化氧化灭活方法。The invention belongs to the technical field of mine ecological restoration, and in particular relates to an in-situ catalytic oxidation inactivation method for acid-producing bacteria by oxidation of iron and sulfur in extremely acidified pyrite soil.
背景技术Background technique
采矿废弃物酸化,在中国乃至世界,都是一个十分严重且日益受到重视的环境问题。大多数有色金属矿以各种类型的金属硫化物存在,如黄铁矿(FeS2)、黄铜矿(CuFeS2)、闪锌矿(ZnS)、方铅矿(PbS)、毒砂(FeAsS)等。裸露矿山中的硫化物等在空气、水和微生物作用下氧化、酸化形成含有大量硫酸盐(1000~130000mg/L)和重金属离子(200~2000mg/L)的高酸性(pH:2.5~6)渗滤液——酸性矿山废水(Acid Mine Drainage,AMD)。AMD一旦产生,过程控制难度大,处理成本高;对城市排水管道存在潜在腐蚀性;进入自然环境后,破坏自然界的碳循环平衡,严重破坏周围的水体、土壤、沉积系统和生态系统。Acidification of mining waste is a very serious and increasingly important environmental problem in China and the world. Most non-ferrous metal ores exist as various types of metal sulfides, such as pyrite (FeS 2 ), chalcopyrite (CuFeS 2 ), sphalerite (ZnS), galena (PbS), arsenopyrite (FeAsS) )Wait. The sulfide in the exposed mine is oxidized and acidified under the action of air, water and microorganisms to form a high acidity (pH: 2.5-6) containing a large amount of sulfate (1000-130000mg/L) and heavy metal ions (200-2000mg/L). Leachate - Acid Mine Drainage (AMD). Once AMD occurs, process control is difficult and the treatment cost is high; it is potentially corrosive to urban drainage pipes; after entering the natural environment, it destroys the natural carbon cycle balance and seriously damages the surrounding water, soil, sedimentary systems and ecosystems.
AMD的主要来源是硫化矿物的氧化,特别是硫铁矿山。黄铁矿(FeS2)是导致AMD产生的主要矿物之一。AMD的产生是物理化学和生物学过程的组合。黄铁矿暴露在外时,在氧气和水的共同作用下发生初步化学氧化(1);随之Fe2+被O2进一步氧化为Fe3+(2),产生的Fe3 +氧化黄铁矿的速度是分子氧速度的18-170倍(3)。即便如此,化学氧化过程仍然非常缓慢。The main source of AMD is the oxidation of sulfide minerals, especially pyrite mines. Pyrite (FeS 2 ) is one of the main minerals that cause AMD. The generation of AMD is a combination of physicochemical and biological processes. When pyrite is exposed to the outside, preliminary chemical oxidation occurs under the combined action of oxygen and water (1); then Fe 2+ is further oxidized by O 2 to Fe 3+ (2), resulting in Fe 3 + oxide pyrite The velocity is 18-170 times that of molecular oxygen (3). Even so, the chemical oxidation process is still very slow.
FeS2+7/2O2+H2O→Fe2++2SO4 2-+2H+ (1)FeS 2 +7/2O 2 +H 2 O→Fe 2+ +2SO 4 2- +2H + (1)
Fe2++1/4O2+H+→Fe3++1/2H2O (2)Fe 2+ +1/4O 2 +H + →Fe 3+ +1/2H 2 O (2)
FeS2+14Fe3++8H2O→15Fe2++2SO4 2-+16H+ (3)FeS 2 +14Fe 3+ +8H 2 O→15Fe 2+ +2SO 4 2- +16H + (3)
地球化学研究证实,自然界中硫铁矿的氧化过程是一个缓慢的化学过程与快速的微生物催化过程。在微生物的催化作用下,Fe2+被快速氧化为Fe3+,将硫铁矿的氧化速率提高了5个数量级。因此,FeS2的酸化过程是主要由微生物催化的间接氧化过程,反应速率极其快速。除此之外,硫铁矿中的硫元素氧化也主要依赖于生物作用,单质硫在酸性环境中的非生物氧化是惰性的,微生物可以直接利用矿山中的还原态硫作为电子供体生长,而产生硫酸,进一步酸化矿山环境。研究证实,在pH 2~3时,铁硫氧化产酸微生物的丰度达到80%~95%,是该环境下的绝对优势物种。因此,该类微生物不仅在硫铁矿氧化、酸化过程中起到了至关重要的作用,也成为极酸性硫铁矿生态修复中的关键阻碍。Geochemical studies have confirmed that the oxidation process of pyrite in nature is a slow chemical process and a fast microbial catalysis process. Under the catalysis of microorganisms, Fe 2+ was rapidly oxidized to Fe 3+ , which increased the oxidation rate of pyrite by 5 orders of magnitude. Therefore, the acidification process of FeS2 is an indirect oxidation process mainly catalyzed by microorganisms, and the reaction rate is extremely fast. In addition, the oxidation of sulfur in pyrite also mainly depends on biological action. The abiotic oxidation of elemental sulfur in an acidic environment is inert, and microorganisms can directly use the reduced sulfur in the mine as an electron donor for growth. It produces sulfuric acid, which further acidifies the mine environment. Studies have confirmed that at pH 2 to 3, the abundance of iron-sulfur oxidation acid-producing microorganisms reaches 80% to 95%, which is the absolute dominant species in this environment. Therefore, such microorganisms not only play a crucial role in the oxidation and acidification of pyrite, but also become a key obstacle in the ecological restoration of extremely acidic pyrite.
微生物与硫铁矿的作用机制可以分为“接触”和“非接触”机制。“接触机制”是指微生物通过其表面的菌毛或分泌物直接吸附于矿物表面,借助自身酶系统直接将金属硫化物晶格氧化溶解成金属离子和SO4 2-。该过程完全不需要依赖和借助Fe3+的作用就可直接将矿物氧化;“非接触机制”通过游离微生物催化体系内的Fe2+快速氧化为Fe3+,而不与硫铁矿直接接触。通常,这两种机制共同存在于硫铁矿的氧化过程。The mechanism of action between microorganisms and pyrite can be divided into "contact" and "non-contact" mechanisms. "Contact mechanism" means that microorganisms directly adsorb on mineral surfaces through pili or secretions on their surfaces, and directly oxidize and dissolve metal sulfide lattices into metal ions and SO 4 2- by means of their own enzyme system. This process can directly oxidize minerals without relying on and relying on the action of Fe 3+ ; the "non-contact mechanism" rapidly oxidizes Fe 2+ to Fe 3+ through free microorganisms in the catalytic system without direct contact with pyrite . Usually, these two mechanisms coexist in the oxidation process of pyrite.
由于AMD对周围生态环境污染极强,有效控制硫铁矿废弃物酸化是一个世界性的难题。目前采用方法主要有物理隔离法和碱性中和法。物理隔离法是在酸性土壤表面覆盖一至数层惰性材料,形成低渗透性密封层、水分隔离层、防止冲蚀层等隔离层,这种方法通常造价很高,当矿地面积较大时难以实现。Due to the strong pollution of AMD to the surrounding ecological environment, it is a worldwide problem to effectively control the acidification of pyrite waste. At present, the main methods used are physical isolation method and alkaline neutralization method. The physical isolation method is to cover one to several layers of inert materials on the surface of the acidic soil to form isolation layers such as low permeability sealing layer, moisture isolation layer, and anti-erosion layer. accomplish.
目前已公开针对极酸化矿山废弃地土壤修复的专利主要采用碱性中和法作为生态重建的前期方法,如中国专利文献(公开号:CN110860554A)在酸化土壤下层施用微生物菌剂,在酸化土壤表层平铺一层石灰和新鲜的农家肥,平衡1~6个月种植足够密度的植物。但该方法通过提高pH仅能沉淀Fe3+,从而抑制部分游离铁硫氧化产酸微生物,对于附着微生物并无明显作用;为了控制反酸,必须向酸化土壤中多次施用石灰,而长期施用石灰不仅增加人力、物力成本,还会造成土壤板结、加速土壤镁和钾的淋失、致使土壤养分不平衡等问题。At present, the patent for soil remediation of extremely acidified mine wasteland has mainly adopted the alkaline neutralization method as the preliminary method of ecological reconstruction. Spread a layer of lime and fresh farmyard manure to balance the plants with sufficient density for 1 to 6 months. However, this method can only precipitate Fe 3+ by increasing the pH, thereby inhibiting part of the free iron-sulfur oxidation and acid-producing microorganisms, and has no obvious effect on the attached microorganisms; in order to control acid reflux, lime must be applied to the acidified soil for many times, and long-term application of lime Lime not only increases labor and material costs, but also causes soil compaction, accelerated soil magnesium and potassium leaching, and caused soil nutrient imbalance.
发明内容SUMMARY OF THE INVENTION
本发明的目的就是为了解决上述问题而提供一种极酸化硫铁矿山土壤中铁硫氧化产酸菌的原位催化氧化灭活方法,能够作为极酸性硫铁矿山生态修复的前处理步骤,避免后续生态修复过程中由于微生物的作用产生的反酸现象,进而提高矿山修复的效率,节约成本。The purpose of the present invention is to provide a kind of in-situ catalytic oxidation inactivation method of iron-sulfur oxidation acid-producing bacteria in extremely acidified pyrite soil in order to solve the above-mentioned problems, which can be used as a pretreatment step for ecological restoration of extremely acid pyrite mines, It avoids the phenomenon of acid reflux caused by the action of microorganisms in the subsequent ecological restoration process, thereby improving the efficiency of mine restoration and saving costs.
本发明的目的通过以下技术方案实现:The object of the present invention is achieved through the following technical solutions:
一种极酸化硫铁矿山土壤中铁硫氧化产酸菌的原位催化氧化灭活方法,对极酸化硫铁矿山土壤进行表面修整,复配氧化药剂,向修整后的矿山土壤0~0.5m深度的土壤中施入复配的氧化药剂并进行翻堆混合,喷洒水,养护3~7天,之后覆盖石灰以调节表层pH值。A method for in-situ catalytic oxidation inactivation of iron-sulfur oxidative acid-producing bacteria in extremely acidified pyrite mine soil. The mixed oxidizing agent was applied to the soil at a depth of m, and the piles were turned and mixed, sprayed with water, cured for 3 to 7 days, and then covered with lime to adjust the pH value of the surface layer.
其中,所述氧化药剂由5~10重量份的次氯酸盐固体与5重量份的稳定剂混合而成。Wherein, the oxidizing agent is prepared by mixing 5-10 parts by weight of solid hypochlorite and 5 parts by weight of stabilizer.
优选地,所述次氯酸盐固体包括次氯酸钠或次氯酸钙固体或其组合,所述稳定剂为氨基酸盐、聚磷酸盐、硅酸钠、滑石粉固体的一种或多种混合物。Preferably, the hypochlorite solid includes sodium hypochlorite or calcium hypochlorite solid or a combination thereof, and the stabilizer is one or more mixtures of amino acid salt, polyphosphate, sodium silicate, and talc solid.
优选地,向修整后的矿山土壤中施入的氧化药剂量为表层0~0.5m矿山土壤干基质量的0.005~0.05%。Preferably, the amount of oxidizing agent applied to the trimmed mine soil is 0.005-0.05% of the dry basis mass of the surface layer 0-0.5 m mine soil.
优选地,向修整后的矿山土壤中喷洒的总水量为矿山土壤干基质量的20~30%。Preferably, the total amount of water sprayed into the trimmed mine soil is 20-30% of the dry basis mass of the mine soil.
优选地,养护过程每天对矿山表层0~0.5m土壤进行翻堆一次,使翻堆后的混合土壤孔隙率在40~50%。Preferably, during the maintenance process, 0-0.5 m of soil on the surface of the mine is turned once a day, so that the porosity of the mixed soil after turning is 40-50%.
优选地,在养护完成后的极酸化硫铁矿山土壤表面覆盖1~2cm的石灰,将表层土壤pH调整至5~8,特别优选为6.5~8Preferably, the surface of the extremely acidified pyrite ore soil after the curing is covered with 1-2 cm of lime, and the pH of the surface soil is adjusted to 5-8, particularly preferably 6.5-8
优选地,所述极酸化硫铁矿山为土壤pH为1.5~3.0的硫铁矿山,并含有磷、硫、铜、铅、锰、锌多种组分的复合矿物。Preferably, the extremely acidified pyrite mine is a pyrite mine with a soil pH of 1.5-3.0, and contains complex minerals of various components of phosphorus, sulfur, copper, lead, manganese and zinc.
优选地,所述极酸化硫铁矿山土壤中铁硫氧化产酸菌含量在5×103~1×109个/g干基。Preferably, the content of iron-sulfur oxidizing acid-producing bacteria in the extremely acidified pyrite soil is 5×10 3 to 1×10 9 cells/g dry basis.
优选地,所述极酸化硫铁矿山土壤中的有机质含量不高于干基的5%,Fe2+浓度为100~500mg/kg。Preferably, the organic matter content in the extremely acidified pyrite soil is not higher than 5% of the dry basis, and the Fe 2+ concentration is 100-500 mg/kg.
优选地,对极酸化硫铁矿山土壤进行表面修整包括去除石头,填补采坑,将土壤表面耕松,深度为40~60cm,修正后的土壤孔隙度40~50%。Preferably, the surface conditioning of the extremely acidified pyrite mine soil includes removing stones, filling mining pits, and plowing the soil surface to a depth of 40-60 cm, and the corrected soil porosity is 40-50%.
本发明选取的次氯酸盐氧化剂,与极酸化矿山土壤环境适配度较高。低pH(1.5~3.0)可以促生HOCl,硫铁矿中的少量Fe2+作为HOCl的天然催化剂,发生类芬顿反应产生活性氧物种,Fe2+与HOCl之间的反应速率比Fe2+与H2O2大3个数量级;无需外加催化剂。The hypochlorite oxidant selected by the present invention has a high degree of adaptation to the extremely acidified mine soil environment. Low pH (1.5~3.0) can promote the growth of HOCl. A small amount of Fe 2+ in pyrite acts as a natural catalyst for HOCl, and a Fenton-like reaction occurs to generate reactive oxygen species. The reaction rate between Fe 2+ and HOCl is higher than that of Fe 2 + is 3 orders of magnitude larger than H2O2 ; no external catalyst is required.
实验室模拟了初始pH值为2.35的FeS2在A.ferrooxidans(亚铁氧化酸硫杆菌,极酸性硫铁矿中最常见的极端嗜酸微生物之一)下的氧化作为对照组;添加本发明中的极酸性硫铁矿生态修复前处理药剂作为实验组。实验组:初始pH为2.35,45d培养后pH为2.32;而对照组,45d培养后pH下降至1.82。The laboratory simulated the oxidation of FeS with an initial pH of 2.35 under A. ferrooxidans ( Thiobacter ferrooxidans, one of the most common extreme acidophilic microorganisms in extremely acidic pyrite) as a control group; adding the present invention The extremely acidic pyrite pretreatment agent in ecological restoration was used as the experimental group. The experimental group: the initial pH was 2.35, and the pH was 2.32 after 45 days of culture; while the control group, the pH dropped to 1.82 after 45 days of culture.
实验室结果说明1)微生物是硫铁矿继续酸化的最主要因素;2)复配氧化药剂可灭活游离和附着铁硫氧化产酸微生物,极大程度上降低极酸性硫铁矿继续酸化的可能,从而避免了施用石灰后的反酸问题。The laboratory results show that 1) microorganisms are the most important factor for the continued acidification of pyrite; 2) the compound oxidizing agent can inactivate free and attached iron-sulfur oxidation and acid-producing microorganisms, greatly reducing the continued acidification of extremely acidic pyrite. possible, thus avoiding the problem of acid reflux after lime application.
与现有技术相比,本发明具有以下有益效果:Compared with the prior art, the present invention has the following beneficial effects:
(1)本发明根据极酸化硫铁矿山土壤中的铁硫氧化微生物的生长特性,采用次氯酸盐原位催化氧化游离和附着的铁硫氧化微生物,解决了碱性石灰中和法容易反酸的问题。经检测,添加本发明中的酸性矿山先导药剂后,游离和附着铁硫氧化微生物均减少99.9%以上。(1) according to the growth characteristics of the iron-sulfur oxidizing microorganisms in the extremely acidified pyrite soil, the present invention adopts the iron-sulfur oxidizing microorganisms that are free and attached to the in-situ catalytic oxidation of hypochlorite, and solves the problem that the alkaline lime neutralization method is easy to acid reflux problem. After testing, after adding the acid mine leading agent in the present invention, both free and attached iron-sulfur oxidizing microorganisms are reduced by more than 99.9%.
(2)本发明通过加入以氨基酸盐、聚磷酸盐、硅酸钠、滑石粉等主要组成成分的稳定剂,提高了前处理药剂的稳定性,避免在搅拌、喷洒、温度升高、阳光直射等条件下HOCl发生分解,保证前处理药剂的效果,并保证施工人员的安全。(2) The present invention improves the stability of the pre-treatment agent by adding the stabilizer with the main components such as amino acid salt, polyphosphate, sodium silicate, talc, etc., avoiding stirring, spraying, temperature rise, direct sunlight Under other conditions, HOCl decomposes to ensure the effect of pretreatment agents and the safety of construction workers.
(3)本发明方法简单,原位催化氧化效果好,尤其适用于极酸化硫铁矿(pH 1.5~3.5);成本低廉,除了基本的氧化药剂和稳定剂外无需额外添加催化剂,避免了外加金属离子造成的成本输入和环境压力。(3) The method of the present invention is simple, the in-situ catalytic oxidation effect is good, and it is especially suitable for extremely acidifying pyrite (pH 1.5-3.5); the cost is low, and no additional catalyst is needed except the basic oxidizing agent and stabilizer, which avoids the need for additional catalysts. Cost inputs and environmental pressures caused by metal ions.
具体实施方式Detailed ways
下面结合具体实施例对本发明进行详细说明,但绝不是对本发明的限制。The present invention will be described in detail below in conjunction with specific embodiments, but by no means limit the present invention.
实施例1Example 1
实施地点位于某硫铁矿酸化尾矿库,该尾矿库是典型黄铁矿(FeS2),选取了1块100m×50m大小的区域作为实验地,与该试验地相邻的1块100m×50m大小的区域作为其对照。该区域土壤原始条件十分恶劣,尾矿pH低至2.52±0.45,土壤酸化程度十分严重,区域内无任何植物生长。采用如下方法步骤对该区域进行治理:The implementation site is located in a pyrite acidified tailings pond. The tailings pond is typical pyrite (FeS 2 ). An area of 100m × 50m was selected as the experimental site, and a 100m block adjacent to the experimental site was selected. An area with a size of ×50m served as its control. The original soil conditions in this area are very bad, the pH of tailings is as low as 2.52±0.45, the degree of soil acidification is very serious, and there is no plant growth in the area. The area is governed by the following method steps:
(1)对极酸化矿山土壤进行表面修整,去除石头,填补采坑。(1) Surface trimming of extremely acidified mine soil, removal of stones, and filling of mining pits.
(2)在该试验地土壤表面耕松深度为0.5m,根据修复工艺要求的含水率计算得该批次酸化尾矿库的加水量为2500m3;将次氯酸钠固体(工业级,有效物质含量25%~35%)5.0吨,氨基酸盐2.5吨混合得到复配氧化药剂。将该药剂与正在翻混的矿山土壤混合,并向该区域喷洒2500m3水。养护5d后(每天翻混,保证土壤孔隙度40~50%)在土壤表层覆盖1.5cm的石灰,将表层土壤pH调整为7.02。分别在施用复配药剂前、养护5d后、覆盖石灰半年(涵盖雨季)后,取样检测pH、铁硫产酸微生物数量。所测结果如表1所示。(2) the soil surface ploughing depth is 0.5m in this test site, and the water addition amount of this batch of acidified tailings pond is calculated according to the moisture content required by the repair process to be 2500m 3 ; %~35%) 5.0 tons, and 2.5 tons of amino acid salts are mixed to obtain a compound oxidizing agent. Mix the agent with the mine soil being tumbled and spray 2500m 3 of water on the area. After 5 days of curing (mixing every day to ensure soil porosity of 40-50%), 1.5 cm of lime was covered on the soil surface, and the pH of the surface soil was adjusted to 7.02. Samples were taken to detect pH and the number of iron-sulfur acid-producing microorganisms before applying the compound agent, after curing for 5 days, and after covering with lime for half a year (covering the rainy season). The measured results are shown in Table 1.
表1极酸化硫铁矿山土壤对照组与实验组指标对比Table 1 Comparison of indicators of extremely acidified pyrite mine soil between the control group and the experimental group
如表1所示,施用复配氧化药剂5d后,铁硫氧化产酸微生物的灭活效率高达99.98%,同时由于次氯酸钠本身pH呈现碱性,配制为氧化药剂后,将极酸化硫铁矿区土壤的pH提高至3.02;而其对照组在此期间pH和铁硫氧化产酸微生物并未发生明显变化。将两块实验区域覆盖石灰半年后,需说明此期间涵盖了的雨季,对照组pH由7.02下降至3.65,铁硫氧化产酸微生物仍然为4.5×105,发生明显反酸现象;实验组的pH稳定在6.98,铁硫氧化产酸微生物为1.5×102。实验组停止继续酸化,并且未发生反酸现象。As shown in Table 1, after applying the compound oxidizing agent for 5 days, the inactivation efficiency of the iron-sulfur oxidation acid-producing microorganism was as high as 99.98%. The pH of the soil was increased to 3.02; while the pH of the control group and the acid-producing microorganisms of iron-sulfur oxidation did not change significantly during this period. After covering the two experimental areas with lime for half a year, it is necessary to explain the rainy season covered during this period. The pH of the control group dropped from 7.02 to 3.65, and the iron-sulfur oxidation acid-producing microorganisms remained at 4.5×10 5 , and the phenomenon of obvious acid reflux occurred; The pH was stable at 6.98, and the iron-sulfur oxidation acid-producing microorganism was 1.5×10 2 . The experimental group stopped acidification, and no acid reflux phenomenon occurred.
实施例2Example 2
实施地点位于某复合铁矿酸化尾矿库,该尾矿库除含有大量磁铁矿外,还含部分黄铜矿和铅锌矿。选取了1块80m×50m大小的区域作为实验地,与该试验地相邻的1块80m×50m大小的区域作为其对照。该区域土壤原始条件十分恶劣,尾矿pH低至3.02±0.56,土壤酸化程度严重,区域内无任何植物生长。采用如下方法步骤对该区域进行治理:The implementation site is located in a compound iron ore acidified tailings pond, which not only contains a large amount of magnetite, but also some chalcopyrite and lead-zinc ore. An area of 80m × 50m was selected as the experimental site, and an area of 80m × 50m adjacent to the experimental site was selected as its control. The original soil conditions in this area are very bad, the pH of the tailings is as low as 3.02±0.56, the soil acidification degree is serious, and there is no plant growth in the area. The area is governed by the following method steps:
(1)对极酸化矿山土壤进行表面修整,去除石头,填补采坑。(1) Surface trimming of extremely acidified mine soil, removal of stones, and filling of mining pits.
(2)在该试验地土壤表面耕松深度为0.5m,根据修复工艺要求的含水率计算得该批次酸化尾矿库的加水量为2000m3;将次氯酸钙固体(工业级,有效氯含量30%~38%)4.0吨,氨基酸盐2.0吨混合得到复配氧化药剂。将该药剂与正在翻混的矿山土壤混合,并向该区域喷洒2000m3水。养护5d后(每天翻混,保证土壤孔隙度40~50%)在土壤表层覆盖1.5cm的石灰,将表层土壤pH调整为7.82。分别在施用复配药剂前、养护5d后、覆盖石灰半年(涵盖雨季)后,取样检测pH、铁硫产酸微生物数量。所测结果如表2所示。(2) the soil surface ploughing depth is 0.5m in this experimental site, and the water addition amount of this batch of acidified tailings pond is calculated according to the moisture content required by the repair process to be 2000m 3 ; calcium hypochlorite solid (industrial grade, effective The chlorine content is 30% to 38%) 4.0 tons, and the amino acid salt is mixed with 2.0 tons to obtain a compound oxidizing agent. The agent is mixed with the mine soil being tumbled and 2000m3 of water is sprayed on the area. After 5 days of curing (mixing every day to ensure soil porosity of 40-50%), 1.5 cm of lime was covered on the soil surface, and the pH of the surface soil was adjusted to 7.82. Samples were taken to detect pH and the number of iron-sulfur acid-producing microorganisms before applying the compound agent, after curing for 5 days, and after covering with lime for half a year (covering the rainy season). The measured results are shown in Table 2.
表2极酸化硫铁矿山土壤对照组与实验组指标对比Table 2 The index comparison between the control group and the experimental group in the extremely acidified pyrite mine soil
如表2所示,施用复配氧化药剂5d后,铁硫氧化产酸微生物的灭活效率高达99.98%,同时由于次氯酸钠本身pH呈现碱性,配制为氧化药剂后,将极酸化硫铁矿区土壤的pH提高至3.58;而其对照组在此期间pH和铁硫氧化产酸微生物并未发生明显变化。将两块实验区域覆盖石灰半年后,需说明此期间涵盖了雨季,对照组pH由7.82下降至3.96,铁硫氧化产酸微生物仍然为4.1×105,发生明显反酸现象;实验组的pH稳定在7.66,铁硫氧化产酸微生物为3.6×102。实验组停止继续酸化,并且未发生反酸现象。As shown in Table 2, after applying the compound oxidizing agent for 5 days, the inactivation efficiency of the iron-sulfur oxidation acid-producing microorganism was as high as 99.98%. The pH of the soil increased to 3.58; while the control group did not change significantly in pH and iron-sulfur oxidation and acid-producing microorganisms during this period. After the two experimental areas were covered with lime for half a year, it should be noted that the rainy season was covered during this period. The pH of the control group dropped from 7.82 to 3.96, and the iron-sulfur oxidation acid-producing microorganisms remained at 4.1×10 5 , and an obvious acid reflux phenomenon occurred; the pH of the experimental group It was stable at 7.66, and the iron-sulfur oxidation acid-producing microorganism was 3.6×10 2 . The experimental group stopped acidification, and no acid reflux phenomenon occurred.
上述的对实施例的描述是为便于该技术领域的普通技术人员能理解和使用发明。熟悉本领域技术的人员显然可以容易地对这些实施例做出各种修改,并把在此说明的一般原理应用到其他实施例中而不必经过创造性的劳动。因此,本发明不限于上述实施例,本领域技术人员根据本发明的揭示,不脱离本发明范畴所做出的改进和修改都应该在本发明的保护范围之内。The foregoing description of the embodiments is provided to facilitate understanding and use of the invention by those of ordinary skill in the art. It will be apparent to those skilled in the art that various modifications to these embodiments can be readily made, and the generic principles described herein can be applied to other embodiments without inventive step. Therefore, the present invention is not limited to the above-mentioned embodiments, and improvements and modifications made by those skilled in the art according to the disclosure of the present invention without departing from the scope of the present invention should all fall within the protection scope of the present invention.
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US5286522A (en) * | 1992-11-19 | 1994-02-15 | University Of Kentucky Research Foundation | H2 O2 induced oxidation proof phosphate surface coating on iron sulfides |
WO2017152795A1 (en) * | 2016-03-09 | 2017-09-14 | 大连地拓重工有限公司 | Resource mine repairing method |
CN110860554A (en) * | 2019-12-05 | 2020-03-06 | 广东桃林生态环境有限公司 | Improvement method for extremely acidified mine soil |
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US5286522A (en) * | 1992-11-19 | 1994-02-15 | University Of Kentucky Research Foundation | H2 O2 induced oxidation proof phosphate surface coating on iron sulfides |
WO2017152795A1 (en) * | 2016-03-09 | 2017-09-14 | 大连地拓重工有限公司 | Resource mine repairing method |
CN110860554A (en) * | 2019-12-05 | 2020-03-06 | 广东桃林生态环境有限公司 | Improvement method for extremely acidified mine soil |
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邱廷省 等: "次氯酸钠水溶液的稳定方法" * |
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