WO2020000372A1 - Combined treatment method for sorghum bicolor (linn.) moench plants rich in heavy metals - Google Patents

Combined treatment method for sorghum bicolor (linn.) moench plants rich in heavy metals Download PDF

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WO2020000372A1
WO2020000372A1 PCT/CN2018/093681 CN2018093681W WO2020000372A1 WO 2020000372 A1 WO2020000372 A1 WO 2020000372A1 CN 2018093681 W CN2018093681 W CN 2018093681W WO 2020000372 A1 WO2020000372 A1 WO 2020000372A1
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combustion
fermentation
fly ash
sweet sorghum
cadmium
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PCT/CN2018/093681
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French (fr)
Chinese (zh)
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李十中
李纪红
薛忠财
仉磊
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清华大学
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    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N1/00Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/14Fungi; Culture media therefor
    • C12N1/16Yeasts; Culture media therefor
    • C12N1/18Baker's yeast; Brewer's yeast
    • C12N1/185Saccharomyces isolates
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00Preparation of oxygen-containing organic compounds
    • C12P7/02Preparation of oxygen-containing organic compounds containing a hydroxy group
    • C12P7/04Preparation of oxygen-containing organic compounds containing a hydroxy group acyclic
    • C12P7/06Ethanol, i.e. non-beverage
    • C12P7/08Ethanol, i.e. non-beverage produced as by-product or from waste or cellulosic material substrate
    • C12P7/10Ethanol, i.e. non-beverage produced as by-product or from waste or cellulosic material substrate substrate containing cellulosic material
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/02Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of bagasse, megasse or the like
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12RINDEXING SCHEME ASSOCIATED WITH SUBCLASSES C12C - C12Q, RELATING TO MICROORGANISMS
    • C12R2001/00Microorganisms ; Processes using microorganisms
    • C12R2001/645Fungi ; Processes using fungi
    • C12R2001/85Saccharomyces
    • C12R2001/865Saccharomyces cerevisiae
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel

Definitions

  • the invention relates to the field of environmental restoration of heavy metal polluted farmland, in particular to a method for jointly treating sweet sorghum plants rich in heavy metals, and belongs to the field of comprehensive recovery and utilization of plant resources and environmental protection.
  • Phytoremediation refers to the use of plants with strong ability to accumulate heavy metals.
  • the heavy metals are transferred and stored in the above-ground part of the plant through absorption and transport.
  • the purpose of reducing the heavy metal content in the soil is achieved by harvesting the above-ground part.
  • Sweet sorghum (Sorghum bicolor (Linn.) Moench), as an important energy plant, has the characteristics of high photosynthetic efficiency, high biological yield, strong resistance to stress, wide adaptability, etc., and it is very useful for heavy metals such as zinc, arsenic, copper, and cadmium. Strong absorption capacity and tolerance, can produce 5-6 tons of stalks with sugar content of 12-14% per mu. Therefore, the production of ethanol from sweet sorghum is considered to be one of the potential alternatives to petroleum. Its mature fermentation process, short production cycle, and relatively low production cost have the advantages.
  • sweet sorghum can be planted on heavy metal-contaminated farmland, if a large amount of sweet sorghum stalk fermentation residues rich in heavy metals such as cadmium cannot be disposed of as quickly and reasonably as possible, it will probably return to the soil. High activity increases its harmfulness and causes secondary pollution.
  • the disposal methods for rehabilitated plants are mainly used as waste or as resources, mainly including incineration, composting, compression landfilling, pyrolysis, plant metallurgy, spices extraction, and bioenergy.
  • the technology for producing ethanol by using sweet sorghum fermentation has been relatively mature, mainly including liquid fermentation method and direct solid-state fermentation method of crushing stalks and squeezing juice.
  • liquid fermentation is the most commonly used method for biofuel ethanol
  • the liquid fermentation process of sweet sorghum stalks has the disadvantages of difficult juice extraction and serious water pollution problems, and basically cannot control the discharge of trace heavy metals in wastewater.
  • the stalk is pulverized.
  • the fermented seed liquid is mixed and mixed to produce ethanol.
  • solid-state fermentation technology improves sugar utilization, simplifies the process, reduces production costs, and avoids the generation of a large amount of wastewater.
  • the energy utilization of the repaired sweet sorghum can be achieved through the production of ethanol, but how to properly handle the large amount of cadmium-rich sweet sorghum stalk fermentation residues produced after fermentation has become a key issue, and the economics of the processing technology And environmental protection is also of great significance to the development of this phytoremediation technology. Therefore, based on the principles of reduction, harmlessness and recycling, incineration is considered to be the most feasible technology.
  • the purpose of the present invention is to provide a combined treatment method for sweet sorghum plants rich in heavy metals, which uses solid-state fermentation technology to treat the stalks to produce fuel ethanol, and then uses combustion technology to treat the heavy metal-rich fermentation residues produced after fermentation. , Generates heat energy and heavy metal-rich residues and fly ash, and finally collects the residues and fly ash for heavy metal recovery.
  • the resource utilization and energy utilization of sweet sorghum plants rich in heavy metals were realized.
  • the reduction and harmless treatment of sweet sorghum stalks were achieved.
  • the solid-state fermentation technology is used to produce ethanol fuel from the stalks of sweet sorghum as raw materials.
  • the specific steps are as follows:
  • the fresh sweet sorghum stalk is peeled and pulverized and mixed uniformly, preferably, the stalk is pulverized to a diameter of 1-5 mm and a length of less than 50 mm;
  • the seed liquid is Saccharomyces cerevisiae Hansen TSH2.
  • the Saccharomyces cerevisiae TSH2 is a special strain that has been specially domesticated and genetically modified. TSH2 can withstand high temperatures under solid fermentation conditions and absorb fermentable sugars. The rate is high, so the solid fermentation efficiency is significantly higher than other industrial yeasts. It is a high-yield ethanol yeast strain, which effectively solves the problems of the previous strains for solid fermentation fermentation heat accumulation (high temperature) and poor mass transfer effect.
  • Ethanol is obtained after distillation of crudely distilled ethanol, and the ethanol yield reaches more than 90%, which further effectively shortens the fermentation time from 24 hours to 20 hours in the prior art.
  • the combustion technology is used to treat sweet sorghum stalk fermentation residues and waste.
  • the combustion technology uses a tube furnace combustion technology.
  • the combustion system includes a gas distribution system, a tube furnace, a fly ash collection system, and flue gas absorption. System composition
  • the gas distribution system includes a gas bottle, a valve, and a gas flow meter for controlling the gas flow rate.
  • the tube furnace uses a SK2-4-10 high temperature tube furnace as a burner, and the furnace temperature can be arbitrarily set at 500-1200 ° C according to the needs of the experiment.
  • the fly ash collection system includes a filter cartridge support and a glass fiber filter cartridge arranged in the support; the glass fiber filter cartridge in the filter cartridge support is used to filter and collect fly ash generated by combustion.
  • the flue gas absorption system includes a series of absorption bottles, and the absorption bottle contains a mixed solution of 5% HNO 3 + 10% H 2 O 2 for absorbing gaseous heavy metals.
  • the combustion technology is used to burn the sweet sorghum stalk fermentation residue and waste at a combustion temperature of 900 ° C to recover cadmium.
  • the specific operation method is:
  • a circulating fluidized bed boiler can be used for combustion treatment of sweet sorghum rod fermentation slag, and the combustion residues and fly ash are collected at a combustion temperature of 900 ° C to maximize the recovery of cadmium; Before the combustion treatment, the sweet sorghum stalk fermentation residue also needs to be dehydrated. The water content in the sweet sorghum stalk fermentation residue after distillation is about 80%. The sweet sorghum is combined with solar energy and heat generated by the combustion of a circulating fluidized bed boiler. The straw fermentation residue is dried to reduce the water content to below 50%.
  • the invention provides a combined treatment method for sweet sorghum plants rich in heavy metals, which uses solid state fermentation technology to ferment sweet sorghum stalks to produce economically valuable ethanol.
  • the selected Saccharomyces cerevisiae TSH2 is used to guarantee an ethanol yield of more than 90%
  • the fermentation time is further shortened; a large amount of cadmium-rich sweet sorghum stalk fermentation slag produced after fermentation is treated by using combustion technology, and the combustion temperature is controlled to maximize the recovery of cadmium in burned fly ash and slag
  • thermal energy with economic value is generated.
  • FIG. 1 is a flow chart of specific steps of a combined treatment method for sweet sorghum plants rich in heavy metals according to the present invention.
  • FIG. 2 is a combustion curve of sweet sorghum stalk fermentation residue at a temperature rising rate of 30 ° C / min.
  • Figure 3 shows the change in the mass of the residue and fly ash (Figure 3a) and its percentage of the total mass ( Figure 3b) after combustion at different temperatures.
  • Figure 4 shows the migration and transformation characteristics of cadmium during the combustion process, of which Figure 4a is the mass of cadmium in the residue, fly ash and smoke; Figure 4b is the normalized distribution of cadmium in the residue, fly ash and smoke; Figure 4c is Cadmium content in residues and fly ash.
  • FIG. 1 is a flow chart of specific steps of a combined treatment method for sweet sorghum plants rich in heavy metals according to the present invention.
  • the present invention provides a combined treatment method for sweet sorghum plants rich in heavy metals.
  • the stalks are treated by wastewater-free solid-state fermentation technology, and crude ethanol is distilled to obtain fuel ethanol.
  • Combustion technology is used to treat the rich Heavy metal fermentation slag produces economical thermal energy and heavy metal-rich residues and fly ash for heavy metal recovery.
  • the resource utilization and energy utilization of sweet sorghum plants rich in heavy metals were realized.
  • the reduction and harmless treatment of sweet sorghum stalks were achieved.
  • Example 1 Solid-state fermentation technology of sweet sorghum stalks
  • the sweet sorghum used in the experiment was grown in a cadmium-contaminated farmland in Shaoguan, Guangdong.
  • the cadmium concentration in the soil was 7.93 mg / kg
  • the effective cadmium content was 2.89 mg / kg
  • the sugar content of the stalk was 11.3%
  • the fresh weight was 750 g / plant.
  • Adopt advanced solid fermentation (ASSF) technology and a unique high temperature resistant, high metabolic efficiency strain (Saccharomyces cerevisiae Hansen TSH2), the main fermentation time is completed within 20 hours, the ethanol yield is more than 90%, and the entire process It produces almost no waste water and effectively reduces secondary pollution of heavy metals.
  • the specific operation method is as follows: the fresh sweet sorghum stem is peeled and pulverized and mixed uniformly (1-5 mm in diameter and less than 50 mm in length), 10 kg of crushed material is weighed, and the cultivated seed liquid is inserted according to 10% of the inoculation amount (
  • the strain is Saccharomyces cerevisiae Hansen (TSH2).
  • the initial fermentation temperature is 25-35 ° C.
  • the fermentation is carried out in a drum fermentation tank with a capacity of 50L.
  • the stirring speed is controlled at 0.08 rpm, and the fermentation is performed for 20 hours. Ethanol is obtained after distillation.
  • the theoretical yield of ethanol is over 90%, and the fermentation time is shortened from 24 hours to 20 hours in the prior art.
  • the strains used in this embodiment are obtained after screening, domestication and genetic modification, and can tolerate the characteristics of high temperature and low mass transfer rate under solid fermentation, further reducing the fermentation time from 24h to 20h in the prior art, thereby improving Fermentation efficiency and ethanol yield.
  • the strain is Saccharomyces cerevisiae TSH2, and the deposit number is CGMCC 14223, and the deposit unit is: General Microbial Center of China Microbial Strain Collection Management Committee, and the deposit date is June 6, 2017.
  • Example 2 Combustion technology of sweet sorghum stalk fermentation residue and waste
  • the combustion system consists of gas distribution system, tube furnace, fly ash collection system and flue gas absorption system.
  • the gas distribution system consists of gas bottles, valves and gas flow meters to control the gas flow rate.
  • the tube furnace uses SK2-4-10 high temperature tube furnace as the burner, and the furnace temperature can be arbitrarily set at 500-1200 ° C according to the needs of the experiment.
  • the fly ash produced by the combustion is collected by filtering through the glass fiber filter cartridge in the cartridge holder.
  • the flue gas absorption system is composed of a series of absorption bottles containing a mixed solution of 5% HNO 3 + 10% H 2 O 2 for absorbing gaseous heavy metals.
  • the specific operation method is: accurately weigh 4.000g sweet sorghum stalk fermentation slag, and study the migration and transformation of cadmium at different combustion temperatures, and set the combustion temperature to 600 ° C, 700 ° C, 800 ° C, 900 ° C, and 1000 ° C for 5 combustion temperatures.
  • the tube furnace is heated up. When the furnace temperature reaches the set temperature, air is passed in and the gas flow rate is 5 L / min. Then, the corundum boat containing the reaction sample is pushed in, and it is left for 30 minutes to make it Complete reaction. After the system cools down, collect slag, fly ash and flue gas absorption liquid.
  • the content of cadmium was determined by inductively coupled plasma emission spectrometer (Agilent 7700X, Agilent Technologies, USA). Fly ash sweet sorghum stem after fermenting sludge and co-firing, the residue microwave digestion were digested (CEM-MARS) method, acid digestion system of HNO 3 -HClO 4 -HF (2: 2: 1), the digestion solution volume .
  • CEM-MARS acid digestion system of HNO 3 -HClO 4 -HF (2: 2: 1
  • For the sample of smoke absorption liquid transfer two bottles of 5% HNO 3 + 10% H 2 O 2 absorption liquid to a 500ml volumetric flask according to the EPA METHOD 29 method, and use a constant volume.
  • Figure 2 is the combustion curve of sweet sorghum stalk fermentation residue at a temperature rise rate of 30 ° C / min, where: TGA represents the change in quality, and DTG represents the first-order differential of quality over time. DTA reflects the change of fuel energy during fuel combustion. It can be seen from the figure that the combustion of sweet sorghum stalk fermentation residue can be divided into four stages: preheating and drying, volatilization analysis, volatiles combustion, and coke burnout. The maximum weight loss rate occurs at about 350 ° C, that is, at Volatile combustion stage.
  • Figure 3 shows the changes in the quality of the residue and fly ash under different temperature combustion conditions. It can be seen from Figure 3a that as the temperature increases, the combustion is more sufficient, resulting in a decline in the quality of the residue and fly ash. From Figure 3b, The percentage of its solid sample decreased from 11.2% at 600 ° C to 6.00% at 900 ° C, which indicates that the quality of the sample was significantly reduced after combustion, effectively reducing the sweet sorghum residue and harmless treatment.
  • Figure 4 shows the migration and transformation characteristics of cadmium at different combustion temperatures.
  • Cadmium has a low boiling point and is a volatile heavy metal.
  • Figure 4a is the mass curve of cadmium in slag, fly ash and flue gas at different combustion temperatures. It can be seen from the figure that the mass of cadmium in the residue decreases with increasing temperature, and the mass of cadmium in fly ash varies with As the temperature rises, it first rises and then decreases, and the mass in the flue gas remains unchanged.
  • Figure 4b is a normalized distribution diagram of the mass change of cadmium in slag, fly ash and flue gas at different temperatures. It can be seen from the figure that cadmium is mainly distributed in fly ash, but the mass in flue gas and residue is low. ; Although cadmium is distributed in bottom slag, fly ash, and flue gas, according to the theory of material balance, 100% recovery can be achieved at different temperatures, and it has no significant effect on the normalized distribution of cadmium.
  • Figure 4c shows the content of cadmium in the residue and fly ash. It can be seen from the figure that the content of cadmium in the residue and fly ash changes with increasing temperature.
  • the content of cadmium in the residue at 900 ° C is 2.23 mg / kg.
  • the content in fly ash can reach 63.3mg / kg.
  • a circulating fluidized bed boiler can be used to comb the sweet sorghum rod fermentation slag.
  • the combustion temperature is 900 ° C
  • the residues and fly ash after combustion are collected to maximize the recovery of cadmium, while not recycling cadmium. Pollution to the environment again.
  • the method for recovering cadmium is to realize the recovery of cadmium by a heap leaching method and an electrodeposition technology.
  • the combustion technology can effectively treat sweet sorghum stalk fermentation residues and wastes, generate thermal energy with economic value for ethanol production and power generation or heating, and the recovery rate of heavy metals in residues rich in heavy metals and fly ash can reach 100 %,
  • the combustion temperature is 900 ° C, cadmium is completely recovered, and energy is saved to the maximum; Harm treatment, while also realizing the resource utilization and energy utilization of sweet sorghum plants rich in heavy metals.
  • the invention is to provide a combined treatment method for sweet sorghum plants rich in heavy metals, to realize the safe disposal of sweet sorghum plants rich in heavy metals.
  • the specific method is to use solid-state fermentation technology to treat the stalks to produce ethanol with economic value, and then burn them.
  • the technology treats fermented slags rich in heavy metals produced after fermentation to generate thermal energy with economic value and residues and fly ash that can be used to extract heavy metals.

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Abstract

A combined treatment method for Sorghum bicolor (Linn.) Moench plants rich in heavy metals: first fermenting Sorghum bicolor (Linn.) Moench stalks by using a solid state fermentation technology to produce ethanol with an economic value, wherein specific Saccharomyces cerevisiae TSH2 is selected to ensure that the fermentation time is further shortened while the ethanol yield is more than 90%; and then performing combustion treatment on a large quantity of cadmium-rich fermentation slag of the Sorghum bicolor (Linn.) Moench stalks generated after fermentation, controlling the combustion temperature to recycle fly ash generated after combustion and cadmium in furnace slag to the greatest extent, and moreover, generate heat energy with an economic value for ethanol production, power generation, or heat supply. By effectively integrating the solid state fermentation technology and the combustion technology, the problem on safe treatment of remediation plants can be effectively solved, and the economy and environmental protection properties can be achieved.

Description

一种富含重金属的甜高粱植株联合处置方法Method for jointly treating sweet sorghum plants rich in heavy metals 技术领域Technical field
本发明涉及重金属污染农田的环境修复领域,具体涉及一种富含重金属的甜高粱植株联合处置方法,属于植物资源的综合回收利用和环境保护领域。The invention relates to the field of environmental restoration of heavy metal polluted farmland, in particular to a method for jointly treating sweet sorghum plants rich in heavy metals, and belongs to the field of comprehensive recovery and utilization of plant resources and environmental protection.
背景技术Background technique
植物修复是指利用对重金属富集能力较强的植物,通过吸收和转运将重金属转移并储存在植物地上部分,最终通过收获地上部分达到减少土壤重金属含量的目的,主要包括两种方式:一是利用超累积植物的超强吸收能力,提取土壤中重金属;二是选用生长迅速、生物量较大、富集重金属能力相对较强的非超累积植物提取重金属。Phytoremediation refers to the use of plants with strong ability to accumulate heavy metals. The heavy metals are transferred and stored in the above-ground part of the plant through absorption and transport. Finally, the purpose of reducing the heavy metal content in the soil is achieved by harvesting the above-ground part. There are two main methods: Extract the heavy metals from the soil by using the superabsorbent capacity of the super-accumulating plants. Second, select non-super-accumulating plants that grow rapidly, have large biomass, and have a relatively strong ability to accumulate heavy metals.
研究人员提出在重金属污染的土地上种植生物产量高的能源植物,一方面实现对重金属污染农田的综合利用,扩大能源植物的种植面积,一方面生产生物质能源(如生物燃气、生物乙醇等),产生一定的经济效益,同时可以对土壤中的重金属进行提取修复,达到一举多效的目的,对于受重金属污染农田的农业结构、增加农民收入、加大修复意义和推广范围等均方面有着积极的作用。Researchers have proposed planting energy plants with high biological yields on heavy metal-contaminated land, on the one hand, to achieve comprehensive utilization of heavy metal-polluted farmland, expand the planting area of energy plants, and on the other hand produce biomass energy (such as biogas, bioethanol, etc.) It can generate certain economic benefits, and at the same time, it can extract and repair heavy metals in the soil to achieve the purpose of multi-effects. It has positive effects on the agricultural structure of farmland polluted by heavy metals, increasing farmers' income, increasing the significance of restoration and extension. Role.
甜高粱(Sorghum bicolor(Linn.)Moench)作为重要的能源植物,具有光合效率高、生物产量高、抗逆性强、适应性广等特点,并对锌、砷、铜、镉等重金属具有很强的吸收能力和耐性,可亩产含糖12-14%的茎秆5-6吨。因此甜高粱生产乙醇被认为是极有潜力的替代石油途径之一,其发酵工艺成熟、生产周期短、生产成本相对低廉的优势。Sweet sorghum (Sorghum bicolor (Linn.) Moench), as an important energy plant, has the characteristics of high photosynthetic efficiency, high biological yield, strong resistance to stress, wide adaptability, etc., and it is very useful for heavy metals such as zinc, arsenic, copper, and cadmium. Strong absorption capacity and tolerance, can produce 5-6 tons of stalks with sugar content of 12-14% per mu. Therefore, the production of ethanol from sweet sorghum is considered to be one of the potential alternatives to petroleum. Its mature fermentation process, short production cycle, and relatively low production cost have the advantages.
虽然甜高粱可以在重金属污染农田上进行种植,但是大量富含镉等重金属的甜高粱秆发酵渣如不能尽快、合理地加以处置,将可能重新回到土壤,且由于生物体中的重金属具有更高的活性而增大其危害性从而 造成二次污染。目前,对于修复植物的处置方法主要是作为废弃物或资源化利用,主要包括焚烧法、堆肥法、压缩填埋法、高温分解法、植物冶金、香料提取、生物能源等。Although sweet sorghum can be planted on heavy metal-contaminated farmland, if a large amount of sweet sorghum stalk fermentation residues rich in heavy metals such as cadmium cannot be disposed of as quickly and reasonably as possible, it will probably return to the soil. High activity increases its harmfulness and causes secondary pollution. At present, the disposal methods for rehabilitated plants are mainly used as waste or as resources, mainly including incineration, composting, compression landfilling, pyrolysis, plant metallurgy, spices extraction, and bioenergy.
利用甜高粱发酵产乙醇的技术已经发展的比较成熟,主要包括粉碎茎秆后榨汁的液态发酵方式和直接固态发酵方式。虽然液态发酵是生物燃料乙醇所最常用的方法,然而甜高粱茎秆液态发酵过程中存在榨汁困难、水污染问题严重等缺点,基本上不能控制排放废水的微量重金属。而甜高粱固态发酵则通过对茎秆进行粉碎,在保证甜高粱粉碎料含水量在一定范围内的前提下,接入发酵种子液混匀之后进行发酵产乙醇。与液体发酵相比,固态发酵技术提高了糖利用率,简化了工艺流程,降低了生产成本,避免了大量废水的产生。The technology for producing ethanol by using sweet sorghum fermentation has been relatively mature, mainly including liquid fermentation method and direct solid-state fermentation method of crushing stalks and squeezing juice. Although liquid fermentation is the most commonly used method for biofuel ethanol, the liquid fermentation process of sweet sorghum stalks has the disadvantages of difficult juice extraction and serious water pollution problems, and basically cannot control the discharge of trace heavy metals in wastewater. For sweet sorghum solid fermentation, the stalk is pulverized. Under the premise that the moisture content of the sweet sorghum crushed material is within a certain range, the fermented seed liquid is mixed and mixed to produce ethanol. Compared with liquid fermentation, solid-state fermentation technology improves sugar utilization, simplifies the process, reduces production costs, and avoids the generation of a large amount of wastewater.
综上,通过生产乙醇可以实现对修复后甜高粱的能源利用,但是如何妥善地处理发酵后所产生的大量富镉的甜高粱杆发酵渣便成了一个关键的问题,同时处理工艺的经济性和环保性也对这项植物修复技术的发展具有重要的意义。因此基于减量化、无害化和资源化的原则,焚烧法被认为是最可行的技术。In summary, the energy utilization of the repaired sweet sorghum can be achieved through the production of ethanol, but how to properly handle the large amount of cadmium-rich sweet sorghum stalk fermentation residues produced after fermentation has become a key issue, and the economics of the processing technology And environmental protection is also of great significance to the development of this phytoremediation technology. Therefore, based on the principles of reduction, harmlessness and recycling, incineration is considered to be the most feasible technology.
因此,需要一种能够有效地解决修复植物的安全处置问题,同时兼具经济性和环保性的富含重金属甜高粱植株的联合处理方法。Therefore, there is a need for a combined treatment method for heavy sorghum plants rich in heavy metals that can effectively solve the problem of safe disposal of rehabilitative plants, and is both economical and environmentally friendly.
发明内容Summary of the invention
为了解决上述问题,本发明的目的在于提供一种富含重金属甜高粱植株的联合处理方法,采用固态发酵技术处理茎秆生产燃料乙醇,再通过燃烧技术处理发酵后产生的富含重金属的发酵渣,产生热能和富含重金属的残渣和飞灰,最后收集残渣和飞灰用于对重金属进行回收。通过两种技术的有效联合与集成,实现了富含重金属甜高粱植株的资源化与能源化利用,与此同时,实现了甜高粱茎秆的减量化和无害化处理。In order to solve the above problems, the purpose of the present invention is to provide a combined treatment method for sweet sorghum plants rich in heavy metals, which uses solid-state fermentation technology to treat the stalks to produce fuel ethanol, and then uses combustion technology to treat the heavy metal-rich fermentation residues produced after fermentation. , Generates heat energy and heavy metal-rich residues and fly ash, and finally collects the residues and fly ash for heavy metal recovery. Through the effective combination and integration of the two technologies, the resource utilization and energy utilization of sweet sorghum plants rich in heavy metals were realized. At the same time, the reduction and harmless treatment of sweet sorghum stalks were achieved.
其中所述固态发酵技术用于将甜高粱的茎秆作为原料生产乙醇燃料,其具体步骤为:The solid-state fermentation technology is used to produce ethanol fuel from the stalks of sweet sorghum as raw materials. The specific steps are as follows:
1.在重金属污染的土壤中种植甜高粱,成熟后获得甜高粱地上部分;1. Plant sweet sorghum in soil contaminated by heavy metals, and obtain sweet sorghum aerial parts after maturity;
2.将新鲜甜高粱茎秆剥叶后粉碎混合均匀,优选地,将茎秆粉碎为直径1-5mm,长度小于50mm;2. The fresh sweet sorghum stalk is peeled and pulverized and mixed uniformly, preferably, the stalk is pulverized to a diameter of 1-5 mm and a length of less than 50 mm;
3.称取粉碎料,按照粉碎料质量的5-15%的接种量,接入已培养好的种子液;其中,接种量是根据菌种的繁殖生长及发酵效率等因素决定。3. Weigh the crushed material and insert the cultivated seed liquid according to the inoculation amount of 5-15% of the mass of the crushed material. Among them, the inoculation amount is determined according to the growth and fermentation efficiency of the bacteria.
优选地,所述种子液为酿酒酵母(Saccharomyces cerevisiae Hansen)TSH2,所述酿酒酵母TSH2为经过特殊驯化、遗传改造的特有菌种,TSH2在固体发酵条件下可耐受高温,且吸收可发酵糖速率高效,从而固体发酵效率明显高于其它工业酵母,为高产乙醇酵母菌种,有效解决了以往的菌种针对固体发酵的发酵热累积(高温)、传质效果差的问题。所述酿酒酵母TSH2,保藏编号:CGMCC 14223,保藏单位为中国微生物菌种保藏管理委员会普通微生物中心,保藏日期为2017年06月06日。Preferably, the seed liquid is Saccharomyces cerevisiae Hansen TSH2. The Saccharomyces cerevisiae TSH2 is a special strain that has been specially domesticated and genetically modified. TSH2 can withstand high temperatures under solid fermentation conditions and absorb fermentable sugars. The rate is high, so the solid fermentation efficiency is significantly higher than other industrial yeasts. It is a high-yield ethanol yeast strain, which effectively solves the problems of the previous strains for solid fermentation fermentation heat accumulation (high temperature) and poor mass transfer effect. The Saccharomyces cerevisiae TSH2, the deposit number: CGMCC 14223, the deposit unit is the General Microbiology Center of the China Microbial Strain Collection Management Committee, and the deposit date is June 06, 2017.
4.在30℃条件下,将步骤3中所述物料直接在固体发酵罐中进行固态发酵,即在转鼓式发酵罐中进行发酵,接种量为茎秆质量的10%,发酵时间24h,搅拌转速控制在0.08rpm。4. Under the condition of 30 ° C, directly perform the solid fermentation in the solid fermenter, that is, ferment in the drum fermenter, the inoculation amount is 10% of the stalk mass, and the fermentation time is 24h. The stirring speed was controlled at 0.08 rpm.
5.粗蒸乙醇精馏后得到乙醇,乙醇产率达到90%以上,进一步有效缩短了发酵时间,由现有技术的24h缩短到20h。5. Ethanol is obtained after distillation of crudely distilled ethanol, and the ethanol yield reaches more than 90%, which further effectively shortens the fermentation time from 24 hours to 20 hours in the prior art.
其中所述燃烧技术用于对甜高粱茎秆发酵渣和废弃物进行处理,所述燃烧技术采用管式炉燃烧技术,燃烧系统包括配气系统、管式炉、飞灰收集系统和烟气吸收系统组成;The combustion technology is used to treat sweet sorghum stalk fermentation residues and waste. The combustion technology uses a tube furnace combustion technology. The combustion system includes a gas distribution system, a tube furnace, a fly ash collection system, and flue gas absorption. System composition
所述配气系统,包括气体瓶、阀门和气体流量计,用于控制气体流速。The gas distribution system includes a gas bottle, a valve, and a gas flow meter for controlling the gas flow rate.
优选地,所述管式炉,采用SK2-4-10型高温管式炉作为燃烧器,炉温可在500-1200℃根据实验需要任意设定。Preferably, the tube furnace uses a SK2-4-10 high temperature tube furnace as a burner, and the furnace temperature can be arbitrarily set at 500-1200 ° C according to the needs of the experiment.
所述飞灰收集系统,包括滤筒支架和设置在支架内的玻璃纤维滤筒;滤筒支架内的玻璃纤维滤筒用于过滤收集燃烧产生的飞灰。The fly ash collection system includes a filter cartridge support and a glass fiber filter cartridge arranged in the support; the glass fiber filter cartridge in the filter cartridge support is used to filter and collect fly ash generated by combustion.
所述烟气吸收系统包括一系列吸收瓶,所述吸收瓶内装5%HNO 3+10%H 2O 2的混合液,用于吸收气态的重金属。 The flue gas absorption system includes a series of absorption bottles, and the absorption bottle contains a mixed solution of 5% HNO 3 + 10% H 2 O 2 for absorbing gaseous heavy metals.
其中,采用燃烧技术在燃烧温度为900℃时,对甜高粱茎秆发酵渣和废弃物进行燃烧处理,进行镉的回收,具体操作方法为:Among them, the combustion technology is used to burn the sweet sorghum stalk fermentation residue and waste at a combustion temperature of 900 ° C to recover cadmium. The specific operation method is:
准确称取甜高粱杆发酵渣,燃烧温度设置在900℃,按照设定好的程 序使管式炉升温;当炉温达到设定温度时通入空气,气体流量为5L/min;随后将盛有反应样品的刚玉舟推入,停留30min后,使之完全反应;待系统冷却后,分别收集炉渣、飞灰和烟气吸收液。在燃烧温度为900℃时,飞灰中镉含量最高,此时只需回收收集燃烧后的部分和玻璃纤维滤筒中的飞灰即可实现镉的完全回收,同时最大限度节约能源。Accurately weigh the sweet sorghum stalk fermentation slag, set the combustion temperature at 900 ° C, and heat the tube furnace according to the set program; when the furnace temperature reaches the set temperature, air is passed in and the gas flow is 5L / min; The corundum boat with the reaction sample was pushed in and left for 30 minutes to make it fully react. After the system was cooled, the slag, fly ash and flue gas absorption liquid were collected separately. When the combustion temperature is 900 ° C, the cadmium content in the fly ash is the highest. At this time, only the burned part and the fly ash in the glass fiber filter can be recovered to achieve the complete recovery of cadmium, while maximizing energy savings.
在实际生产中,可选用循环流化床锅炉对甜高粱杆发酵渣进行燃烧处理,燃烧温度为900℃时收集燃烧后的残渣和飞灰以最大限度实现镉的回收;采用所述燃烧技术进行燃烧处理前,还需要对所述甜高粱杆发酵渣进行脱水处理,蒸馏后的甜高粱杆发酵渣中含水量约为80%,联合采用太阳能和循环流化床锅炉燃烧产生的热能对甜高粱杆发酵渣进行干燥处理,使含水量降低到50%以下。In actual production, a circulating fluidized bed boiler can be used for combustion treatment of sweet sorghum rod fermentation slag, and the combustion residues and fly ash are collected at a combustion temperature of 900 ° C to maximize the recovery of cadmium; Before the combustion treatment, the sweet sorghum stalk fermentation residue also needs to be dehydrated. The water content in the sweet sorghum stalk fermentation residue after distillation is about 80%. The sweet sorghum is combined with solar energy and heat generated by the combustion of a circulating fluidized bed boiler. The straw fermentation residue is dried to reduce the water content to below 50%.
本发明提供一种富含重金属甜高粱植株的联合处理方法,采用固态发酵技术对甜高粱茎秆进行发酵生产具有经济价值的乙醇,其中选用的特有的酿酒酵母TSH2在保证乙醇产率90%以上的同时进一步缩短了发酵时间;采用燃烧技术对发酵后所产生的大量富镉的甜高粱茎杆发酵渣进行处理,通过控制燃烧的温度以最大限度的回收燃烧后的飞灰和炉渣中的镉,同时产生具有经济价值的热能,本发明通过固态发酵技术和焚烧技术的有效集成,有效地解决修复植物的安全处置问题,并兼具经济性和环保性。The invention provides a combined treatment method for sweet sorghum plants rich in heavy metals, which uses solid state fermentation technology to ferment sweet sorghum stalks to produce economically valuable ethanol. The selected Saccharomyces cerevisiae TSH2 is used to guarantee an ethanol yield of more than 90% At the same time, the fermentation time is further shortened; a large amount of cadmium-rich sweet sorghum stalk fermentation slag produced after fermentation is treated by using combustion technology, and the combustion temperature is controlled to maximize the recovery of cadmium in burned fly ash and slag At the same time, thermal energy with economic value is generated. Through the effective integration of solid-state fermentation technology and incineration technology, the present invention effectively solves the problem of safe disposal of repaired plants, and is both economical and environmentally friendly.
应当理解,前述大体的描述和后续详尽的描述均为示例性说明和解释,并不应当用作对本发明所要求保护内容的限制。It should be understood that the foregoing general description and the subsequent detailed description are exemplary descriptions and explanations, and should not be used as a limitation on the claimed content of the present invention.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
参考随附的附图,本发明更多的目的、功能和优点将通过本发明实施方式的如下描述得以阐明,其中:With reference to the accompanying drawings, further objects, functions and advantages of the present invention will be clarified by the following description of the embodiments of the present invention, in which:
图1为本发明富含重金属甜高粱植株的联合处理方法的具体步骤流程图。FIG. 1 is a flow chart of specific steps of a combined treatment method for sweet sorghum plants rich in heavy metals according to the present invention.
图2为在30℃/min的升温速率条件下,甜高粱茎秆发酵渣的燃烧曲线。FIG. 2 is a combustion curve of sweet sorghum stalk fermentation residue at a temperature rising rate of 30 ° C / min.
图3为不同温度燃烧后,残渣和飞灰质量(图3a)以及其占总质量 的百分比(图3b)的变化。Figure 3 shows the change in the mass of the residue and fly ash (Figure 3a) and its percentage of the total mass (Figure 3b) after combustion at different temperatures.
图4为燃烧过程中镉的迁移转化特征,其中图4a为镉在残渣、飞灰和烟气中的质量;图4b镉在残渣、飞灰和烟气中的归一化分布;图4c为残渣、飞灰中镉的含量。Figure 4 shows the migration and transformation characteristics of cadmium during the combustion process, of which Figure 4a is the mass of cadmium in the residue, fly ash and smoke; Figure 4b is the normalized distribution of cadmium in the residue, fly ash and smoke; Figure 4c is Cadmium content in residues and fly ash.
具体实施方式detailed description
通过参考示范性实施例,本发明的目的和功能以及用于实现这些目的和功能的方法将得以阐明。然而,本发明并不受限于以下所公开的示范性实施例;可以通过不同形式来对其加以实现。说明书的实质仅仅是帮助相关领域技术人员综合理解本发明的具体细节。The objects and functions of the present invention and methods for achieving the objects and functions will be clarified by referring to the exemplary embodiments. However, the present invention is not limited to the exemplary embodiments disclosed below; it can be implemented in different forms. The essence of the description is merely to help those skilled in the relevant art to comprehensively understand the specific details of the present invention.
在下文中,将参考附图描述本发明的实施例。在附图中,相同的附图标记代表相同或类似的部件,或者相同或类似的步骤。Hereinafter, embodiments of the present invention will be described with reference to the drawings. In the drawings, the same reference numerals represent the same or similar components, or the same or similar steps.
图1为本发明富含重金属甜高粱植株的联合处理方法的具体步骤流程图。参见图1,本发明提供一种富含重金属甜高粱植株的联合处理方法,采用无废水固态发酵技术处理茎秆,粗蒸乙醇精馏后得到燃料乙醇,通过燃烧技术处理发酵后产生的富含重金属的发酵渣,产生具有经济价值的热能和富含重金属的残渣和飞灰,进行重金属的回收。通过两种技术的有效联合与集成,实现了富含重金属甜高粱植株的资源化与能源化利用,与此同时,实现了甜高粱茎秆的减量化和无害化处理。FIG. 1 is a flow chart of specific steps of a combined treatment method for sweet sorghum plants rich in heavy metals according to the present invention. Referring to FIG. 1, the present invention provides a combined treatment method for sweet sorghum plants rich in heavy metals. The stalks are treated by wastewater-free solid-state fermentation technology, and crude ethanol is distilled to obtain fuel ethanol. Combustion technology is used to treat the rich Heavy metal fermentation slag produces economical thermal energy and heavy metal-rich residues and fly ash for heavy metal recovery. Through the effective combination and integration of the two technologies, the resource utilization and energy utilization of sweet sorghum plants rich in heavy metals were realized. At the same time, the reduction and harmless treatment of sweet sorghum stalks were achieved.
实施例1甜高粱茎秆的固态发酵技术Example 1 Solid-state fermentation technology of sweet sorghum stalks
试验所用甜高粱种植于广东韶关的镉污染农田,土壤中的镉浓度为7.93mg/kg,有效镉含量为2.89mg/kg,茎秆含糖量为11.3%,鲜重为750g/株。采用先进固体发酵(ASSF)技术及特有耐高温、高代谢效率菌株(菌种为酿酒酵母(Saccharomyces cerevisiae Hansen)TSH2),实现主发酵时间20h内完成,乙醇产率90%以上,且整个工艺过程几乎不产生废水,有效减少重金属的二次污染。The sweet sorghum used in the experiment was grown in a cadmium-contaminated farmland in Shaoguan, Guangdong. The cadmium concentration in the soil was 7.93 mg / kg, the effective cadmium content was 2.89 mg / kg, the sugar content of the stalk was 11.3%, and the fresh weight was 750 g / plant. Adopt advanced solid fermentation (ASSF) technology and a unique high temperature resistant, high metabolic efficiency strain (Saccharomyces cerevisiae Hansen TSH2), the main fermentation time is completed within 20 hours, the ethanol yield is more than 90%, and the entire process It produces almost no waste water and effectively reduces secondary pollution of heavy metals.
具体操作方法为:将新鲜甜高粱茎秆剥叶后粉碎混合均匀(直径1-5mm,长度小于50mm),称取10kg的粉碎料,按照10%的接种量接入已培养好的种子液(菌种为酿酒酵母(Saccharomyces cerevisiae Hansen)TSH2),初始发酵温度25-35℃,放入容量为50L的转鼓式发酵罐中进 行发酵,搅拌转速控制在0.08rpm,发酵20h,蒸馏后得到乙醇,乙醇理论收率达到90%以上,其中发酵时间由现有技术的24h缩短到20h。The specific operation method is as follows: the fresh sweet sorghum stem is peeled and pulverized and mixed uniformly (1-5 mm in diameter and less than 50 mm in length), 10 kg of crushed material is weighed, and the cultivated seed liquid is inserted according to 10% of the inoculation amount ( The strain is Saccharomyces cerevisiae Hansen (TSH2). The initial fermentation temperature is 25-35 ° C. The fermentation is carried out in a drum fermentation tank with a capacity of 50L. The stirring speed is controlled at 0.08 rpm, and the fermentation is performed for 20 hours. Ethanol is obtained after distillation. The theoretical yield of ethanol is over 90%, and the fermentation time is shortened from 24 hours to 20 hours in the prior art.
本实施例中采用的菌种是经过筛选、驯化及遗传改造后得到,可耐受固体发酵下高温、传质速率低的特点,进一步将发酵时间由现有技术的24h缩短到20h,从而提高发酵效率和乙醇产率。所述菌种为酿酒酵母TSH2,保藏编号为CGMCC 14223,保藏单位为:中国微生物菌种保藏管理委员会普通微生物中心,保藏日期为2017年06月06日。The strains used in this embodiment are obtained after screening, domestication and genetic modification, and can tolerate the characteristics of high temperature and low mass transfer rate under solid fermentation, further reducing the fermentation time from 24h to 20h in the prior art, thereby improving Fermentation efficiency and ethanol yield. The strain is Saccharomyces cerevisiae TSH2, and the deposit number is CGMCC 14223, and the deposit unit is: General Microbial Center of China Microbial Strain Collection Management Committee, and the deposit date is June 6, 2017.
实施例2甜高粱茎秆发酵渣和废弃物的燃烧技术Example 2 Combustion technology of sweet sorghum stalk fermentation residue and waste
采用管式炉燃烧技术,燃烧系统包括配气系统、管式炉、飞灰收集系统和烟气吸收系统组成。配气系统由气体瓶、阀门和气体流量计组成,控制气体流速。管式炉采用SK2-4-10型高温管式炉作为燃烧器,炉温可在500-1200℃根据实验需要任意设定。燃烧产生的飞灰由滤筒支架内的玻璃纤维滤筒过滤收集。烟气吸收系统由一系列吸收瓶组成,内装5%HNO 3+10%H 2O 2的混合液,用于吸收气态的重金属。 Using tube furnace combustion technology, the combustion system consists of gas distribution system, tube furnace, fly ash collection system and flue gas absorption system. The gas distribution system consists of gas bottles, valves and gas flow meters to control the gas flow rate. The tube furnace uses SK2-4-10 high temperature tube furnace as the burner, and the furnace temperature can be arbitrarily set at 500-1200 ° C according to the needs of the experiment. The fly ash produced by the combustion is collected by filtering through the glass fiber filter cartridge in the cartridge holder. The flue gas absorption system is composed of a series of absorption bottles containing a mixed solution of 5% HNO 3 + 10% H 2 O 2 for absorbing gaseous heavy metals.
具体操作方法为:准确称取4.000g甜高粱杆发酵渣,分别研究其在不同燃烧温度下镉的迁移转化,设置为600℃、700℃、800℃、900℃、1000℃共5个燃烧温度,按照设定好的程序使管式炉升温,当炉温达到设定温度时通入空气,气体流量为5L/min,随后将盛有反应样品的刚玉舟推入,停留30min后,使之完全反应,待系统冷却后,分别收集炉渣、飞灰和烟气吸收液。The specific operation method is: accurately weigh 4.000g sweet sorghum stalk fermentation slag, and study the migration and transformation of cadmium at different combustion temperatures, and set the combustion temperature to 600 ° C, 700 ° C, 800 ° C, 900 ° C, and 1000 ° C for 5 combustion temperatures. According to the set program, the tube furnace is heated up. When the furnace temperature reaches the set temperature, air is passed in and the gas flow rate is 5 L / min. Then, the corundum boat containing the reaction sample is pushed in, and it is left for 30 minutes to make it Complete reaction. After the system cools down, collect slag, fly ash and flue gas absorption liquid.
采用电感耦合等离子体发射光谱仪(Agilent 7700X,Agilent Technologies,USA)测定其中镉的含量。对甜高粱杆发酵渣及共燃烧后的飞灰、残渣采用微波消解(CEM-MARS)法进行消解,消解酸体系为HNO 3-HClO 4-HF(2:2:1),消解液定容。对烟气吸收液样品参照EPA METHOD 29方法将两瓶5%HNO 3+10%H 2O 2吸收液转移至500ml容量瓶中,并用定容。 The content of cadmium was determined by inductively coupled plasma emission spectrometer (Agilent 7700X, Agilent Technologies, USA). Fly ash sweet sorghum stem after fermenting sludge and co-firing, the residue microwave digestion were digested (CEM-MARS) method, acid digestion system of HNO 3 -HClO 4 -HF (2: 2: 1), the digestion solution volume . For the sample of smoke absorption liquid, transfer two bottles of 5% HNO 3 + 10% H 2 O 2 absorption liquid to a 500ml volumetric flask according to the EPA METHOD 29 method, and use a constant volume.
参见图2-图4,图2为在30℃/min的升温速率条件下,甜高粱茎秆发酵渣的燃烧曲线,其中:TGA表示质量的变化情况,DTG表示质量对时间的一阶微分,DTA反映燃料燃烧过程中燃料的能量变化情况。由图 可知,甜高粱茎秆发酵渣的燃烧可以分为预热和干燥、挥发分析出、挥发分燃烧、焦炭燃烧燃尽等四个阶段,最大失重速率集中发生在约350℃时,即在挥发分燃烧阶段。See Figures 2 to 4, Figure 2 is the combustion curve of sweet sorghum stalk fermentation residue at a temperature rise rate of 30 ° C / min, where: TGA represents the change in quality, and DTG represents the first-order differential of quality over time. DTA reflects the change of fuel energy during fuel combustion. It can be seen from the figure that the combustion of sweet sorghum stalk fermentation residue can be divided into four stages: preheating and drying, volatilization analysis, volatiles combustion, and coke burnout. The maximum weight loss rate occurs at about 350 ° C, that is, at Volatile combustion stage.
图3为残渣和飞灰质量在不同温度燃烧条件下的变化情况,由图3a可知:随着温度的增加,燃烧更加充分,导致残渣和飞灰的质量呈下降的趋势,由图3b可知,其所占固体样品的百分比由600℃下的11.2%下降到900℃下的6.00%,这说明经过燃烧后,样品质量明显减少,有效实现了甜高粱残渣的减量化和无害化处理。Figure 3 shows the changes in the quality of the residue and fly ash under different temperature combustion conditions. It can be seen from Figure 3a that as the temperature increases, the combustion is more sufficient, resulting in a decline in the quality of the residue and fly ash. From Figure 3b, The percentage of its solid sample decreased from 11.2% at 600 ° C to 6.00% at 900 ° C, which indicates that the quality of the sample was significantly reduced after combustion, effectively reducing the sweet sorghum residue and harmless treatment.
图4表明不同燃烧温度下镉的迁移转化特征。镉的沸点低,是一种易挥发重金属。Figure 4 shows the migration and transformation characteristics of cadmium at different combustion temperatures. Cadmium has a low boiling point and is a volatile heavy metal.
图4a为不同燃烧温度下镉在炉渣、飞灰和烟气中的质量曲线,由图可知,镉在残渣中的质量随着温度的升高而降低,而镉在飞灰中的质量则随着温度的升高先升高再降低,在烟气中的质量则没有变化。Figure 4a is the mass curve of cadmium in slag, fly ash and flue gas at different combustion temperatures. It can be seen from the figure that the mass of cadmium in the residue decreases with increasing temperature, and the mass of cadmium in fly ash varies with As the temperature rises, it first rises and then decreases, and the mass in the flue gas remains unchanged.
图4b为镉在不同温度下在炉渣、飞灰和烟气中的质量变化的归一化分布图,由图可知,镉主要分布在飞灰中,而在烟气和残渣中的质量较低;虽然镉在底渣、飞灰、烟气中均有分布,但是根据物质平衡的理论,不同温度下均可达到100%的回收,并且对镉的归一化分布没有显著影响。Figure 4b is a normalized distribution diagram of the mass change of cadmium in slag, fly ash and flue gas at different temperatures. It can be seen from the figure that cadmium is mainly distributed in fly ash, but the mass in flue gas and residue is low. ; Although cadmium is distributed in bottom slag, fly ash, and flue gas, according to the theory of material balance, 100% recovery can be achieved at different temperatures, and it has no significant effect on the normalized distribution of cadmium.
图4c为残渣、飞灰中镉的含量,由图可知,镉在残渣和飞灰中的含量随着温度的升高呈不同的变化,900℃下在残渣中的镉含量为2.23mg/kg,而在飞灰中含量可达63.3mg/kg。Figure 4c shows the content of cadmium in the residue and fly ash. It can be seen from the figure that the content of cadmium in the residue and fly ash changes with increasing temperature. The content of cadmium in the residue at 900 ° C is 2.23 mg / kg. , And the content in fly ash can reach 63.3mg / kg.
综上可知:在900℃温度下燃烧,飞灰中镉含量最高,此时只需收集燃烧后残渣和飞灰即可实现镉的回收,同时最大限度节约能源,也避免了在低温下燃烧会产生二恶英的问题。In summary, it is known that when burning at 900 ° C, the cadmium content in fly ash is the highest. At this time, only the residue and fly ash after the combustion can be collected to achieve the recovery of cadmium. At the same time, it saves energy to the greatest extent and avoids burning at low temperatures. Dioxin problems.
在实际生产中,可采用循环流化床锅炉对甜高粱杆发酵渣进行燃烧处理,所述燃烧温度为900℃时,收集燃烧后的残渣和飞灰以最大限度实现镉的回收,同时不会再次对环境造成污染。所述镉回收的方法为通过堆浸法和电沉积技术实现镉的回收。In actual production, a circulating fluidized bed boiler can be used to comb the sweet sorghum rod fermentation slag. When the combustion temperature is 900 ° C, the residues and fly ash after combustion are collected to maximize the recovery of cadmium, while not recycling cadmium. Pollution to the environment again. The method for recovering cadmium is to realize the recovery of cadmium by a heap leaching method and an electrodeposition technology.
所述燃烧技术能够有效处理甜高粱茎秆发酵渣和废弃物,产生具有 经济价值的热能用于乙醇生产及发电或供热,对于富含重金属的残渣和飞灰中的重金属回收率可达到100%,实际生产中,在保证甜高粱茎秆发酵渣充分燃烧的情况下,在燃烧温度为900℃时,镉完全回收,同时最大限度节约能源;实现了甜高粱茎秆的减量化和无害化处理,同时还实现了富含重金属甜高粱植株的资源化与能源化利用。The combustion technology can effectively treat sweet sorghum stalk fermentation residues and wastes, generate thermal energy with economic value for ethanol production and power generation or heating, and the recovery rate of heavy metals in residues rich in heavy metals and fly ash can reach 100 %, In actual production, under the condition that the fermentation residues of sweet sorghum stalks are fully burned, when the combustion temperature is 900 ° C, cadmium is completely recovered, and energy is saved to the maximum; Harm treatment, while also realizing the resource utilization and energy utilization of sweet sorghum plants rich in heavy metals.
本发明在于提供一种富含重金属甜高粱植物的联合处理方法,实现对富含重金属甜高粱植株的安全处置,具体的方法是采用固态发酵技术处理茎秆产生有经济价值的乙醇,再通过燃烧技术处理发酵后产生的富含重金属的发酵渣,产生具有经济价值的热能和可用于提取重金属的残渣和飞灰。通过两种技术的有效联合与集成,实现了富含重金属甜高粱植株的资源化与能源化利用,与此同时,实现了甜高粱茎秆的减量化和无害化处理。The invention is to provide a combined treatment method for sweet sorghum plants rich in heavy metals, to realize the safe disposal of sweet sorghum plants rich in heavy metals. The specific method is to use solid-state fermentation technology to treat the stalks to produce ethanol with economic value, and then burn them. The technology treats fermented slags rich in heavy metals produced after fermentation to generate thermal energy with economic value and residues and fly ash that can be used to extract heavy metals. Through the effective combination and integration of the two technologies, the resource utilization and energy utilization of sweet sorghum plants rich in heavy metals were realized. At the same time, the reduction and harmless treatment of sweet sorghum stalks were achieved.
结合这里披露的本发明的说明和实践,本发明的其他实施例对于本领域技术人员都是易于想到和理解的。说明和实施例仅被认为是示例性的,本发明的真正范围和主旨均由权利要求所限定。In conjunction with the description and practice of the invention disclosed herein, other embodiments of the invention will be readily conceivable and understood by those skilled in the art. The description and examples are to be considered exemplary only, with the true scope and spirit of the invention being defined by the claims.

Claims (8)

  1. 一种富含重金属甜高粱植株的联合处理方法,采用无废水的固态发酵技术处理茎秆,粗蒸乙醇精馏后得到燃料乙醇,对发酵后产生的富含重金属的发酵渣进行脱水处理后采用燃烧技术进行处理,产生热能和含有重金属的残渣和飞灰,最后收集的残渣和飞灰用于重金属回收提取。A combined treatment method for sweet sorghum plants rich in heavy metals. The stalks are treated by solid-state fermentation technology without waste water. Crude steamed ethanol is rectified to obtain fuel ethanol. The heavy metal-rich ferment residues produced after fermentation are dehydrated and used. Combustion technology is used for processing to generate thermal energy and residues and fly ash containing heavy metals. The collected residues and fly ash are used for heavy metal recovery and extraction.
  2. 根据权利要求1所述的联合处理方法,所述采用无废水固态发酵技术处理茎秆的具体步骤为:The combined treatment method according to claim 1, wherein the specific steps for treating the stalks by using wastewater-free solid state fermentation technology are:
    步骤一,在重金属污染的土壤中种植甜高粱,成熟后获得甜高粱地上部分;Step 1: Plant sweet sorghum in soil contaminated by heavy metals, and obtain sweet sorghum aerial parts after maturity;
    步骤二,将新鲜甜高粱茎秆剥叶后粉碎混合均匀,将茎秆粉碎为直径1-5mm,长度小于50mm;Step 2: The fresh sweet sorghum stem is peeled and pulverized and mixed uniformly, and the stem is pulverized to a diameter of 1-5 mm and a length of less than 50 mm;
    步骤三,称取粉碎料,按照粉碎料质量的5-15%的接种量,接入已培养好的种子液;Step 3: Weigh the crushed material, and insert the cultivated seed liquid according to the inoculation amount of 5-15% of the mass of the crushed material;
    步骤四,在30℃条件下,将步骤三中所述物料直接在固体发酵罐中进行固态发酵,即在转鼓式发酵罐中进行发酵,接种量为茎秆质量的10%,发酵时间20h,搅拌转速控制在0.08rpm;Step 4: Under the condition of 30 ° C, directly perform the solid fermentation in the solid fermenter, that is, ferment in the drum fermenter, the inoculation amount is 10% of the stem mass, and the fermentation time is 20h. , The stirring speed is controlled at 0.08rpm;
    步骤五,粗蒸乙醇精馏后得到乙醇,乙醇产率达到90%以上。Step 5: Ethanol is obtained after crude distillation of ethanol, and the ethanol yield is above 90%.
  3. 根据权利要求2所述的联合处理方法,在步骤三中,所述种子液为酿酒酵母TSH2,保藏编号:CGMCC 14223,保藏单位为中国微生物菌种保藏管理委员会普通微生物中心,保藏日期为2017年06月06日。The method of claim 2, in step 3, the seed liquid is Saccharomyces cerevisiae TSH2, the deposit number is CGMCC 14223, and the deposit unit is the Ordinary Microbiology Center of the China Microbial Strain Collection Management Committee, and the preservation date is 2017. June 06.
  4. 根据权利要求1所述的联合处理方法,所述燃烧技术采用管式炉燃烧技术,其燃烧系统包括配气系统、管式炉、飞灰收集系统和烟气吸收系统组成;The combined processing method according to claim 1, wherein the combustion technology uses a tube furnace combustion technology, and the combustion system comprises a gas distribution system, a tube furnace, a fly ash collection system, and a flue gas absorption system;
    所述配气系统,包括气体瓶、阀门和气体流量计,用于控制气体流速;The gas distribution system includes a gas bottle, a valve, and a gas flow meter for controlling a gas flow rate;
    所述管式炉,采用SK2-4-10型高温管式炉作为燃烧器,炉温可在500-1200℃任意设定;The tube furnace uses a SK2-4-10 high temperature tube furnace as a burner, and the furnace temperature can be arbitrarily set at 500-1200 ° C;
    所述飞灰收集系统,包括滤筒支架和设置在支架内的玻璃纤维滤筒; 滤筒支架内的玻璃纤维滤筒用于过滤收集燃烧产生的飞灰;The fly ash collection system includes a filter cartridge support and a glass fiber filter cartridge arranged in the support; the glass fiber filter cartridge in the filter cartridge support is used to filter and collect fly ash generated by combustion;
    所述烟气吸收系统包括一系列吸收瓶,所述吸收瓶内装5%HNO 3+10%H 2O 2的混合液,用于吸收气态的重金属。 The flue gas absorption system includes a series of absorption bottles, and the absorption bottle contains a mixed solution of 5% HNO 3 + 10% H 2 O 2 for absorbing gaseous heavy metals.
  5. 根据权利要求4所述的联合处理方法,采用所述燃烧技术在燃烧温度为900℃时,对甜高粱茎秆发酵渣和废弃物进行燃烧处理,进行镉的回收,具体操作方法为:The combined treatment method according to claim 4, wherein the combustion technology is used to combust sweet sorghum stalk fermentation residue and waste at a combustion temperature of 900 ° C to recover cadmium, and the specific operation method is:
    准确称取甜高粱杆发酵渣,燃烧温度设置在900℃,按照设定好的程序使管式炉升温;当炉温达到设定温度时通入空气,气体流量为5L/min;随后将盛有反应样品的刚玉舟推入,停留30min后,使之完全反应;待系统冷却后,分别收集炉渣、飞灰和烟气吸收液;在燃烧温度为900℃时,飞灰中镉含量最高,收集残渣和飞灰用于重金属镉回收提取。Accurately weigh the sweet sorghum stalk fermentation slag, set the combustion temperature at 900 ° C, and heat the tube furnace according to the set program; when the furnace temperature reaches the set temperature, air is passed in and the gas flow is 5L / min; The corundum boat with the reaction sample was pushed in and left to react for 30 minutes. After the system was cooled, the slag, fly ash and flue gas absorption liquid were collected separately. When the combustion temperature was 900 ° C, the cadmium content in the fly ash was the highest. Collect the residue and fly ash for heavy metal cadmium recovery and extraction.
  6. 根据权利要求1所述的联合处理方法,所述燃烧技术选用循环流化床锅炉对甜高粱杆发酵渣进行燃烧处理,燃烧温度为900℃时收集燃烧后的残渣和飞灰以最大限度实现镉的回收。The combined treatment method according to claim 1, wherein the combustion technology uses a circulating fluidized bed boiler to burn sweet sorghum rod fermentation slag, and collects burned residues and fly ash at a combustion temperature of 900 ° C to maximize cadmium Recycling.
  7. 根据权利要求6所述的联合处理方法,所述燃烧技术进行燃烧处理前,联合采用太阳能和循环流化床锅炉燃烧产生的热能对甜高粱杆发酵渣进行脱水处理,使含水量从80%降低到50%以下。The combined treatment method according to claim 6, before the combustion technology performs the combustion treatment, the sweet sorghum stalk fermentation residue is dehydrated by using solar energy and thermal energy generated by the combustion of a circulating fluidized bed boiler to reduce the water content from 80% To below 50%.
  8. 根据权利要求5或6所述的联合处理方法,所述重金属镉回收采用的方法为堆浸法和电沉积技术。The method according to claim 5 or 6, wherein the method for recovering the heavy metal cadmium is a heap leaching method and an electrodeposition technology.
PCT/CN2018/093681 2018-06-29 2018-06-29 Combined treatment method for sorghum bicolor (linn.) moench plants rich in heavy metals WO2020000372A1 (en)

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102399826A (en) * 2011-10-20 2012-04-04 清华大学 Comprehensive utilizing method of sweet sorghum stalks
RU2499954C1 (en) * 2012-06-06 2013-11-27 Общество с ограниченной ответственностью "КИВИ Энерджи" Method to produce thermal and electric energy from renewable sources
CN104324933A (en) * 2014-11-04 2015-02-04 清华大学 Comprehensive repair method of heavy metal contaminated soil and application
CN107631307A (en) * 2017-07-13 2018-01-26 清华大学 A kind of sugar grass plant joint method of disposal rich in heavy metal

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102399826A (en) * 2011-10-20 2012-04-04 清华大学 Comprehensive utilizing method of sweet sorghum stalks
RU2499954C1 (en) * 2012-06-06 2013-11-27 Общество с ограниченной ответственностью "КИВИ Энерджи" Method to produce thermal and electric energy from renewable sources
CN104324933A (en) * 2014-11-04 2015-02-04 清华大学 Comprehensive repair method of heavy metal contaminated soil and application
CN107631307A (en) * 2017-07-13 2018-01-26 清华大学 A kind of sugar grass plant joint method of disposal rich in heavy metal

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