CN115521814A - Method for bonding and pressing regenerated fuel by using medical waste - Google Patents
Method for bonding and pressing regenerated fuel by using medical waste Download PDFInfo
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/46—Solid fuels essentially based on materials of non-mineral origin on sewage, house, or town refuse
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
- C10L5/04—Raw material of mineral origin to be used; Pretreatment thereof
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- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
- C10L5/06—Methods of shaping, e.g. pelletizing or briquetting
- C10L5/10—Methods of shaping, e.g. pelletizing or briquetting with the aid of binders, e.g. pretreated binders
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
- C10L5/26—After-treatment of the shaped fuels, e.g. briquettes
- C10L5/28—Heating the shaped fuels, e.g. briquettes; Coking the binders
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
- C10L5/34—Other details of the shaped fuels, e.g. briquettes
- C10L5/36—Shape
- C10L5/361—Briquettes
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- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
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- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
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Abstract
本发明提供一种利用医疗废物粘合压制再生燃料的方法,包括:步骤S1,利用双级双轴撕碎机对医疗废物进行撕碎处理;步骤S2,将撕碎后的医疗废物送入研磨粉碎设备;步骤S3,将研磨后的医疗废物送入磁选设备;步骤S4,将筛选后的医疗废渣提升至缓存装置进行存放;步骤S5,将缓存装置中的医疗废物传输至搅拌设备,向搅拌设备内添加粘合剂并搅拌均匀;步骤S6,将掺入粘合剂并充分搅拌后的医疗废物送入成型设备。将干化学处理后的医疗废物粘合压制成燃料块,便于医疗废物运输,避免了环境污染,提高了医疗废物衍生燃料的热值,实现了医疗废物的资源化利用,降低了处置费用,具有良好的经济效益和环境效益。
The invention provides a method for bonding and pressing recycled fuel by using medical waste, comprising: step S1, shredding medical waste by using a two-stage double-shaft shredder; step S2, sending the shredded medical waste into grinding crushing equipment; step S3, send the ground medical waste to the magnetic separation equipment; step S4, lift the screened medical waste to the buffer device for storage; step S5, transfer the medical waste in the buffer device to the stirring device, and send it to the A binder is added into the stirring device and stirred evenly; step S6, the medical waste mixed with the binder and fully stirred is sent to the molding device. The dry chemically treated medical waste is bonded and pressed into fuel blocks, which facilitates the transportation of medical waste, avoids environmental pollution, improves the calorific value of medical waste-derived fuels, realizes the resource utilization of medical waste, and reduces disposal costs. Good economic and environmental benefits.
Description
技术领域technical field
本发明属于医废回收技术领域,具体涉及一种利用医疗废物粘合压制再生燃料的方法。The invention belongs to the technical field of medical waste recycling, and in particular relates to a method for bonding and pressing recycled fuel by using medical waste.
背景技术Background technique
医疗垃圾是医疗机构在医疗、预防和保健等活动中产生的具有感染性、毒性以及其他危害性的废弃物,医疗废物成分复杂,包括感染性、病理性、损伤性和药物性以及化学性废物等,涉及塑料、玻璃、金属和人体组织等。传统医疗废物的处理方法有焚烧、高温灭菌、微波灭菌、干化学消毒等方式。干化学消毒法是将粉碎的医疗废物与化学消毒剂混合,并在封闭系统或负压下反应一段时间,在这个过程中,医疗废物中的感染性微生物被灭活或杀死,最终实现医疗废物的无害化处置。Medical waste is infectious, toxic and other hazardous waste produced by medical institutions in the activities of medical treatment, prevention and health care. The composition of medical waste is complex, including infectious, pathological, injurious and pharmaceutical and chemical waste etc., involving plastic, glass, metal and human tissue. Traditional medical waste treatment methods include incineration, high temperature sterilization, microwave sterilization, and dry chemical disinfection. The dry chemical disinfection method is to mix crushed medical waste with a chemical disinfectant and react for a period of time in a closed system or under negative pressure. During this process, the infectious microorganisms in the medical waste are inactivated or killed, and finally achieve medical treatment Harmless disposal of waste.
目前,干化学法工艺简单,处置效率高,废气产生量小,可有效缓解疫情带来的医疗废物处置压力。然而干化学法并未实现医疗废物减量化,处置后的医疗废物通常被送往生活垃圾焚烧厂进一步焚烧,对于医疗废物处置企业来说增加了处置成本,散装医疗废物运输不便,在运途中极易抛撒,对环境造成极大威胁。干化学医疗废物中的金属杂质,会降低热值,增加灰分。若能将干化学医疗废物进行筛分加工制作成垃圾衍生燃料,则可有效解决以上问题。At present, the dry chemical method has a simple process, high disposal efficiency, and a small amount of waste gas, which can effectively alleviate the pressure of medical waste disposal caused by the epidemic. However, the dry chemical method has not achieved the reduction of medical waste, and the disposed medical waste is usually sent to domestic waste incineration plants for further incineration, which increases the disposal cost for medical waste disposal enterprises, and the transportation of bulk medical waste is inconvenient. It is easy to be thrown and poses a great threat to the environment. Metal impurities in dry chemical medical waste will reduce calorific value and increase ash content. If the dry chemical medical waste can be sieved and processed into garbage-derived fuel, the above problems can be effectively solved.
发明内容Contents of the invention
本发明的目的是克服上述现有技术中的不足,提供一种利用医疗废物粘合压制再生燃料的方法。The purpose of the present invention is to overcome the deficiencies in the above-mentioned prior art, and provide a method of using medical waste to bind and press recycled fuel.
为了实现上述目的,本发明提供如下技术方案:In order to achieve the above object, the present invention provides the following technical solutions:
一种利用医疗废物粘合压制再生燃料的方法,包括:A method of binding and pressing recycled fuel from medical waste, comprising:
步骤S1,利用双级双轴撕碎机对医疗废物进行撕碎处理,并在撕碎过程中向医疗废物中添加消毒粉,使医疗废物与消毒粉充分混合;Step S1, shredding the medical waste with a two-stage, two-shaft shredder, and adding disinfection powder to the medical waste during the shredding process, so that the medical waste and the disinfection powder are fully mixed;
步骤S2,将撕碎后的医疗废物送入研磨粉碎设备,再次加入消毒粉,进行充分混合;Step S2, send the shredded medical waste to the grinding and crushing equipment, add disinfection powder again, and fully mix;
步骤S3,将研磨后的医疗废物送入磁选设备,通过磁选筛出医疗废物中的金属制品;Step S3, sending the ground medical waste into a magnetic separation device, and screening out the metal products in the medical waste through magnetic separation;
步骤S4,将筛选后的医疗废渣提升至缓存装置进行存放,使消毒粉与医废进行充分反应;Step S4, lifting the screened medical waste residue to the buffer device for storage, so that the disinfection powder and the medical waste can fully react;
步骤S5,将缓存装置中的医疗废物传输至搅拌设备,向搅拌设备内添加粘合剂并搅拌均匀;Step S5, transfer the medical waste in the buffer device to the stirring device, add adhesive to the stirring device and stir evenly;
步骤S6,将掺入粘合剂并充分搅拌后的医疗废物送入成型设备,通过成型设备挤压成型,将成型后的医疗废物送入微波烘干设备进行烘干,送入打包设备进行打包。Step S6, send the medical waste mixed with the adhesive and fully stirred into the molding equipment, extruded by the molding equipment, send the molded medical waste to the microwave drying equipment for drying, and send it to the packaging equipment for packaging .
优选地,其特征在于,步骤S1中所添加的消毒粉重量为医疗废物重量的2%~3%;步骤S2中所添加的消毒粉重量为医疗废物重量的6%~8%。Preferably, it is characterized in that the weight of the disinfection powder added in step S1 is 2%-3% of the weight of medical waste; the weight of disinfection powder added in step S2 is 6%-8% of the weight of medical waste.
优选地,所述消毒粉为生石灰和粉煤灰的混合物,其中,生石灰与粉煤灰的质量比为5:1~2:1;Preferably, the disinfection powder is a mixture of quicklime and fly ash, wherein the mass ratio of quicklime to fly ash is 5:1 to 2:1;
生石灰的比表面积>300m2/kg,粉煤灰的比表面积>500m2/kg,经双级双轴撕碎机破碎后的医疗废物最大粒径<10cm;经研磨粉碎设备破碎后的医疗废物粒径<5cm。The specific surface area of quicklime > 300m 2 /kg, the specific surface area of fly ash > 500m 2 /kg, the maximum particle size of the medical waste crushed by the two-stage twin-shaft shredder is <10cm; the medical waste crushed by the grinding and crushing equipment Particle size <5cm.
优选地,步骤S5所述粘合剂包括以下组份的原料,羟丙基甲基纤维素的重量份数为0.02~0.1份,工业预糊化淀粉的重量份数为1~3份、硼砂的重量份数为0.05~0.2份,造纸黑液的重量份数为2~10份;Preferably, the binder described in step S5 includes raw materials of the following components, the parts by weight of hydroxypropyl methylcellulose are 0.02 to 0.1 parts by weight, the parts by weight of industrial pregelatinized starch are 1 to 3 parts by weight, borax The parts by weight are 0.05 to 0.2 parts, and the parts by weight of papermaking black liquor are 2 to 10 parts;
所述工业预糊化淀粉水分含量<9%,灰分<0.5%,糊化度>55%;The moisture content of the industrial pregelatinized starch is <9%, the ash content is <0.5%, and the degree of gelatinization is >55%;
所述羟丙基甲基纤维素粘度为100000~200000mPa·s;The viscosity of the hydroxypropyl methylcellulose is 100,000 to 200,000 mPa·s;
所述硼砂中四硼酸钠含量>95%;The content of sodium tetraborate in the borax is >95%;
所述造纸黑液中木质素和半纤维素浓度为25%~60%,造纸黑液粘度<1000mPa·s。The concentration of lignin and hemicellulose in the papermaking black liquor is 25%-60%, and the viscosity of the papermaking black liquor is less than 1000mPa·s.
优选地,在医疗废物挤压成型前,先加入按照比例混合后的羟丙基甲基纤维素、工业预糊化淀粉和硼砂,以60~100r/min转速对粘合剂和医疗废物进行搅拌混合,搅拌时间为1~20min后,将造纸黑液喷洒至医疗废物上,继续搅拌1~10min。Preferably, before the medical waste is extruded, add hydroxypropyl methylcellulose, industrial pregelatinized starch and borax mixed in proportion, and stir the adhesive and medical waste at a speed of 60-100r/min Mixing, after stirring for 1-20 minutes, spray the papermaking black liquor on the medical waste, and continue stirring for 1-10 minutes.
优选地,步骤S6,医疗废物的成型压力为2MPa~20MPa,成型温度为 10~40℃,保压时间5~25s,成型后的医疗废物为圆柱形或棱柱形,横截面积为1~64cm2,长度为2~20cm;微波烘干所采用的微波功率>10KW,烘干时间为10s~1800s,使烘干后燃料棒含水率<10%。Preferably, in step S6, the molding pressure of medical waste is 2MPa-20MPa, the molding temperature is 10-40°C, and the holding time is 5-25s. The medical waste after molding is cylindrical or prismatic, with a cross-sectional area of 1-64cm 2. The length is 2-20cm; the microwave power used for microwave drying is >10KW, and the drying time is 10s-1800s, so that the moisture content of the fuel rod after drying is <10%.
优选地,双级双轴撕碎机、研磨粉碎设备、缓存装置、搅拌设备、微波烘干设备、挤压成型设备和打包设备对应设置在封闭仓内,Preferably, the two-stage two-shaft shredder, the grinding and crushing equipment, the buffer device, the stirring equipment, the microwave drying equipment, the extrusion molding equipment and the packaging equipment are correspondingly arranged in the closed warehouse,
抽风机分别通过抽风管道将封闭仓内的废气导向空气净化装置,所述空气净化装置与抽风机的出气口之间设有冷凝器;The exhaust fan guides the waste gas in the closed warehouse to the air purification device through the exhaust duct respectively, and a condenser is arranged between the air purification device and the air outlet of the exhaust fan;
所述空气净化装置至少包括布袋除尘器、UV光催化氧化装置和活性炭吸附装置。The air purification device at least includes a bag filter, a UV photocatalytic oxidation device and an activated carbon adsorption device.
优选地,双级双轴撕碎机包括:Preferably, the two-stage twin-shaft shredder includes:
进料仓,所述进料仓侧部设置进料口,在所述进料口处设置闸板,所述闸板通过驱动装置驱动,在所述进料口设有感应装置,所述感应装置和所述驱动装置对应连接在控制器上;A feed bin, a feed port is provided on the side of the feed bin, a gate is set at the feed port, the gate is driven by a driving device, an induction device is provided at the feed port, and the induction The device and the driving device are correspondingly connected to the controller;
破碎机构,两个所述破碎机构沿纵向间隔分布在进料仓下方,两个所述破碎机构之间通过导料嘴连通,位于上方的所述破碎机构对应连通所述进料仓下端;A crushing mechanism, the two crushing mechanisms are longitudinally spaced below the feed bin, and the two crushing mechanisms are connected through a feed nozzle, and the upper crushing mechanism is correspondingly connected to the lower end of the feed bin;
所述破碎机构包括刀箱和主轴,两个所述主轴平行分布在所述刀箱内,每个所述主轴上均设有多个动刀,两个所述主轴上的所述动刀交错设置;The crushing mechanism includes a knife box and a main shaft, and the two main shafts are distributed in the knife box in parallel, and each of the main shafts is provided with a plurality of moving knives, and the moving knives on the two main shafts are staggered set up;
同一所述主轴上,任意相邻两个所述动刀之间均设有耐磨盘,在所述刀箱的两侧设有对应所述耐磨盘的定刀,所述定刀内侧免倾斜延伸至刀箱内壁的上沿;On the same main shaft, wear-resistant discs are provided between any two adjacent moving knives, and fixed knives corresponding to the wear-resistant discs are arranged on both sides of the knife box, and the inside of the fixed knives is free from extending obliquely to the upper edge of the inner wall of the knife box;
在所述动刀周向均匀分布有多个刀刃,相邻两个动刀之间的所述刀刃错位设置;There are a plurality of blades evenly distributed in the circumferential direction of the moving knife, and the blades between two adjacent moving knives are arranged in a misalignment;
导料嘴上设有投放口,用于投放消毒粉。The feeding nozzle is provided with a feeding port for feeding the disinfectant powder.
优选地,研磨粉碎设备包括:Preferably, the grinding and crushing equipment includes:
研磨电机,研磨电机连接减速机,减速机连接研磨螺旋,研磨螺旋边缘设有螺旋研磨齿;Grinding motor, the grinding motor is connected to the reducer, the reducer is connected to the grinding spiral, and the edge of the grinding spiral is provided with spiral grinding teeth;
外壳,外壳上设有进料口、出料口、检修口,外壳内壁设有外壳研磨齿,螺旋研磨齿与外壳研磨齿互嵌并留有间隙,间隙为5~10mm。The shell, the shell is provided with a material inlet, a material outlet, and an inspection port. The inner wall of the shell is provided with shell grinding teeth. The spiral grinding teeth and the shell grinding teeth are interlocked with a gap, and the gap is 5-10mm.
优选地,缓存装置的主体为料塔,所述料塔内部设有料位监测模块、温度检测模块和pH检测模块,在所述料塔下方设置有重量检测装置,料塔的底部设有对应连接输料器的出口;Preferably, the main body of the buffer device is a material tower, and a material level monitoring module, a temperature detection module and a pH detection module are arranged inside the material tower, a weight detection device is arranged below the material tower, and a corresponding connection is provided at the bottom of the material tower the outlet of the feeder;
在料塔外壁设有夹层,料塔内腔设有多组在纵向上均匀分布的换热管,所述换热管的两端穿过所述料塔对应连通所述夹层,所述夹层上设有进液口和出液口,向所述夹层内循环供入热介质,以对医废进行加热;There is an interlayer on the outer wall of the material tower, and the inner cavity of the material tower is provided with multiple groups of heat exchange tubes that are evenly distributed in the longitudinal direction. The two ends of the heat exchange tubes pass through the material tower and communicate with the interlayer correspondingly. A liquid inlet and a liquid outlet are provided to circulate heat medium into the interlayer to heat medical waste;
在所述料塔的出口处设有风嘴,所述风嘴对应连接热风装置。An air nozzle is provided at the outlet of the material tower, and the air nozzle is correspondingly connected with a hot air device.
有益效果:1.经过撕碎机和研磨粉碎设备的破碎,将大块不规则的医疗废物破碎为细小颗粒,一方面有利于与消毒粉混合,实现病菌充分消杀,另一方面便于挤压成型。Beneficial effects: 1. After being crushed by shredders and grinding and crushing equipment, large pieces of irregular medical waste are broken into fine particles. On the one hand, it is beneficial to mix with disinfection powder to fully disinfect germs, and on the other hand, it is convenient to squeeze forming.
2.消毒粉中的生石灰在遇水后,反应生热,促进了医疗废物中的病菌消杀,同时,压制成燃料块后,在燃烧过程中,石灰可以吸收部分燃烧废气中的氯化氢,从而减轻废气处置压力。粉煤灰的掺入,一方面起到阻隔作用,另一方面粉煤灰中含有大量玻璃微珠,具有润滑作用,从而避免医疗废物在破碎粉磨过程中相互粘连,促使医疗废物与消毒粉更均匀混合2. After the quicklime in the disinfection powder meets water, it reacts to generate heat, which promotes the sterilization of germs in the medical waste. At the same time, after being pressed into a fuel block, the lime can absorb part of the hydrogen chloride in the combustion exhaust gas during the combustion process, thereby Reduce the pressure of exhaust gas disposal. The incorporation of fly ash, on the one hand, acts as a barrier, and on the other hand, the fly ash contains a large number of glass beads, which have a lubricating effect, thereby preventing medical waste from sticking to each other during the crushing and grinding process, and promoting the separation of medical waste and disinfection powder. more evenly mixed
3.粘合剂的加入有利于破碎后的干化学医疗废物低压成型,所制备粘合剂特别适用于干化学医疗废物的粘结,从而稍加压力即可成型,节约了挤压成型能耗,同时,成型后的燃料块热值提高,便于运输和燃烧。3. The addition of adhesive is beneficial to the low-pressure molding of crushed dry chemical medical waste. The prepared adhesive is especially suitable for the bonding of dry chemical medical waste, so that it can be formed with a little pressure, saving the energy consumption of extrusion molding , At the same time, the calorific value of the formed fuel block is increased, which is convenient for transportation and combustion.
4.微波烘干效率高、速度快,并先从核心发热,逐步辐射外围,烘干效果良好,烘干后的燃料块热值可进一步提高。4. Microwave drying has high efficiency and fast speed, and heats up from the core first, and gradually radiates to the periphery. The drying effect is good, and the calorific value of the dried fuel block can be further improved.
5.将干化学处理后的医疗废物粘合压制成燃料块,便于医疗废物运输,避免了环境污染,提高了医疗废物衍生燃料的热值,实现了医疗废物的资源化利用,降低了处置费用,具有良好的经济效益和环境效益。5. Bond and press dry chemically treated medical waste into fuel blocks, which facilitates the transportation of medical waste, avoids environmental pollution, improves the calorific value of medical waste-derived fuels, realizes resource utilization of medical waste, and reduces disposal costs , has good economic and environmental benefits.
附图说明Description of drawings
构成本申请的一部分的说明书附图用来提供对本发明的进一步理解,本发明的示意性实施例及其说明用于解释本发明,并不构成对本发明的不当限定。其中:The accompanying drawings constituting a part of the present application are used to provide a further understanding of the present invention, and the schematic embodiments and descriptions of the present invention are used to explain the present invention, and do not constitute an improper limitation of the present invention. in:
图1为本发明所提供具体实施例中生产线的示意图;Fig. 1 is the schematic diagram of production line in the specific embodiment provided by the present invention;
图2为本发明所提供具体实施例中双级双轴撕碎机的结构简图;Fig. 2 is a schematic structural diagram of a two-stage two-shaft shredder in a specific embodiment provided by the present invention;
图3为本发明所提供具体实施例中双级双轴撕碎机的内部结构简图;Fig. 3 is a schematic diagram of the internal structure of the two-stage two-shaft shredder in the specific embodiment provided by the present invention;
图4为本发明所提供具体实施例中缓存装置的结构简图;FIG. 4 is a schematic structural diagram of a cache device in a specific embodiment provided by the present invention;
图5为本发明所提供具体实施例中粘结剂粘结后的微观图;Figure 5 is a microscopic view of the bonding agent in the specific embodiment provided by the present invention;
图6为本发明所提供具体实施例中研磨粉碎设备的结构简图;Fig. 6 is a schematic structural diagram of grinding and crushing equipment in a specific embodiment provided by the present invention;
图7为本发明所提供具体实施例中螺旋研磨齿与外壳研磨齿的配合示意图。Fig. 7 is a schematic diagram of cooperation between the spiral grinding teeth and the housing grinding teeth in the specific embodiment provided by the present invention.
图中:1、双级双轴撕碎机、2、缓存装置;3、研磨粉碎设备;4、成型设备;5、微波烘干设备;6、打包设备;7、磁选装置;8、提升装置;9、传送设备;10、立式搅拌桶;11、封闭仓;12、支管;13、抽风机;14、冷凝器;15、空气净化装置;101、进料仓;102、闸板;103、撕碎电机;104、导料嘴;105、投放口;106、刀箱;107、动刀;108、主轴;109、定刀;110、耐磨盘;201、夹层;202、换热管;203、温度检测模块;204、pH检测模块; 205、重量检测装置;206、料位监测模块;207、风嘴;301、研磨电机;302、减速机;303、进料口;304、研磨螺旋;305、外壳;306、检修口;307、出料口;308、螺旋研磨齿;309、外壳研磨齿。In the figure: 1. Two-stage two-shaft shredder, 2. Cache device; 3. Grinding and crushing equipment; 4. Forming equipment; 5. Microwave drying equipment; 6. Packing equipment; 7. Magnetic separation device; 8. Lifting Device; 9. Transmission equipment; 10. Vertical mixing tank; 11. Closed warehouse; 12. Branch pipe; 13. Exhaust fan; 14. Condenser; 15. Air purification device; 101. Feed bin; 102. Gate; 103, shredding motor; 104, material guide nozzle; 105, feeding port; 106, knife box; 107, moving knife; 108, main shaft; 109, fixed knife; 110, wear-resistant disc; 201, interlayer; 202, heat exchange Tube; 203, temperature detection module; 204, pH detection module; 205, weight detection device; 206, material level monitoring module; 207, air nozzle; 301, grinding motor; 302, reducer; Grinding spiral; 305, shell; 306, inspection port; 307, discharge port; 308, spiral grinding teeth; 309, shell grinding teeth.
具体实施方式detailed description
下面将对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明的一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below, obviously, the described embodiments are only some of the embodiments of the present invention, not all of the embodiments. All other embodiments obtained by persons of ordinary skill in the art based on the embodiments of the present invention belong to the protection scope of the present invention.
在本发明的描述中,术语“纵向”、“横向”、“上”、“下”、“前”、“后”、“左”、“右”、“竖直”、“水平”、“顶”、“底”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本发明而不是要求本发明必须以特定的方位构造和操作,因此不能理解为对本发明的限制。本发明中使用的术语“相连”、“连接”应做广义理解,例如,可以是固定连接,也可以是可拆卸连接;可以是直接相连,也可以通过中间部件间接相连,对于本领域的普通技术人员而言,可以根据具体情况理解上述术语的具体含义。In the description of the present invention, the terms "longitudinal", "transverse", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", " The orientations or positional relationships indicated by "top", "bottom", etc. are based on the orientations or positional relationships shown in the drawings, and are only for the convenience of describing the present invention and do not require that the present invention must be constructed and operated in a specific orientation, so they cannot be understood as Limitations on the Invention. The terms "connected" and "connected" used in the present invention should be understood in a broad sense, for example, it can be fixedly connected or detachably connected; it can be directly connected or indirectly connected through intermediate parts, for ordinary A skilled person can understand the specific meanings of the above terms according to specific situations.
下面将参考附图并结合实施例来详细说明本发明。需要说明的是,在不冲突的情况下,本发明中的实施例及实施例中的特征可以相互组合。The present invention will be described in detail below with reference to the accompanying drawings and examples. It should be noted that, in the case of no conflict, the embodiments of the present invention and the features in the embodiments can be combined with each other.
如图1-7所示,一种利用医疗废物粘合压制再生燃料的方法,包括:步骤S1,利用双级双轴撕碎机1对医疗废物进行撕碎处理,医疗废物经过双级双轴撕碎机1撕裂粉碎,有利于与消毒粉混合和挤压成型,具体在撕碎过程中向医疗废物中消毒粉,在撕碎过程中能够使医疗废物与消毒粉充分混合;步骤S2,撕碎后的医疗废物送入研磨粉碎设备3,通过研磨粉碎设备3使医疗废物破碎为更小颗粒,在该过程中再次加入消毒粉,使破碎后的医疗废物与消毒粉更加充分混合;步骤S3,将研磨后的医疗废物送入磁选设备,通过磁选筛出医疗废物中的金属制品;该磁选设备可以为电磁盘式除铁器、永磁自卸式除铁器均可,对应设置在医疗废物生产线的传送设备7上,以此在医疗废物经过磁选设备时,将金属制品进行筛选,一方面可以对金属制品进行回收,另一方面避免金属制品影响最终成品的质量;步骤S4,将破碎后的医疗废渣提升至缓存装置2进行存放,在缓存装置2内存放一定时间,使消毒剂与医废进行充分反应,具体的医疗废物在缓存装置2内存放的时间可以为 2小时;步骤S5,将缓存装置2中的医疗废物传输至搅拌设备,向搅拌设备内添加粘合剂并搅拌均匀;粘合剂的加入有利于破碎后的干化学医疗废物低压成型,所制备粘合剂特别适用于干化学医疗废物的粘结,从而稍加压力即可成型;步骤S6,将掺入粘合剂并充分搅拌后的医疗废物送入成型设备4,通过成型设备4挤压成型,之后送入微波烘干设备5进行烘干,微波烘干设备5可以是隧道式微波烘干机,微波烘干效率高、速度快,并先从核心发热,逐步辐射外围,烘干效果良好,烘干后的燃料块热值可进一步提高,烘干完成后送入打包设备6进行打包,打包设备6可以是自动装袋机。在本实施例中,搅拌设备为立式搅拌桶10,双级双轴撕碎机1通过提升装置8进行上料。As shown in Figure 1-7, a method for bonding and pressing recycled fuel by using medical waste, including: step S1, shredding the medical waste by using a double-stage double-shaft shredder 1, and the medical waste passes through a double-stage double-shaft shredder The shredder 1 shreds and shreds, which is conducive to mixing and extruding with disinfection powder. Specifically, during the shredding process, the disinfection powder is added to the medical waste, and the medical waste and the disinfection powder can be fully mixed during the shredding process; step S2, The shredded medical waste is sent to the grinding and crushing equipment 3, and the medical waste is broken into smaller particles through the grinding and crushing equipment 3, and the disinfection powder is added again in the process, so that the crushed medical waste and the disinfection powder are more fully mixed; steps S3, send the ground medical waste to the magnetic separation equipment, and screen out the metal products in the medical waste through magnetic separation; On the
在另一可选实施例中,步骤S1中所添加的消毒粉重量为医疗废物重量的2%-3%,具体可以为2%、2.5%或3%;步骤S3中所添加的消毒粉重量为医疗废物重量的6%-8%,具体可以为6%、7%、7.5%或8%;In another optional embodiment, the weight of disinfection powder added in step S1 is 2%-3% of the weight of medical waste, specifically 2%, 2.5% or 3%; the weight of disinfection powder added in step S3 6%-8% of the weight of medical waste, specifically 6%, 7%, 7.5% or 8%;
最优的在步骤S1中所添加的消毒粉重量为医疗废物重量的2.5%,步骤 S3中所添加的消毒粉重量为医疗废物重量的7.5%,以此添加消毒粉的重量为医疗废物重量的十分之一。在本实施例中,消毒粉为生石灰和粉煤灰的混合物,其中,生石灰与粉煤灰的质量比为5:1~2:1,例如:生石灰5重量份、粉煤灰1重量份;生石灰4重量份、粉煤灰1重量份;生石灰3重量份、粉煤灰1重量份;生石灰2重量份、粉煤灰1重量份;消毒粉中的生石灰在遇到医疗废物内的水分后,反应生热,促进了医疗废物中的病菌消杀,同时,医疗废物压制成燃料块后,在燃烧过程中,石灰可以吸收部分燃烧废气中的氯化氢,从而减轻废气处置压力。粉煤灰的掺入,一方面起到阻隔作用,另一方面粉煤灰中含有大量玻璃微珠,具有润滑作用,从而避免医疗废物在破碎粉磨过程中相互粘连,促使医疗废物与消毒粉更均匀混合。在一实施例中,生石灰的比表面积>300m2/kg,粉煤灰的比表面积>500m2/kg,为保证充分的消毒,在缓存装置2内存放的时间为2小时,以此保证医疗废物的消毒时间,在本实施例中,通过加入消毒粉使消毒反应时pH值为11.0~12.5;经双级双轴撕碎机1破碎后的医疗废物最大粒径<10cm;经研磨粉碎设备3破碎后的医疗废物为絮状物,其粒径<5cm,双级双轴撕碎机1在进行撕裂过程中,消毒粉反应生热与研磨粉碎过程中摩擦生热使物料反应温度>45℃,进一步增强了消杀效果,整体消毒时间≥125min,能够保证消毒效果。The optimal weight of the added disinfectant powder in step S1 is 2.5% of the weight of medical waste, and the weight of added disinfectant powder in step S3 is 7.5% of the weight of medical waste. one tenth. In this embodiment, the disinfection powder is a mixture of quicklime and fly ash, wherein the mass ratio of quicklime to fly ash is 5:1 to 2:1, for example: 5 parts by weight of quicklime and 1 part by weight of fly ash; 4 parts by weight of quicklime, 1 part by weight of fly ash; 3 parts by weight of quicklime, 1 part by weight of flyash; 2 parts by weight of quicklime, 1 part by weight of flyash; after the quicklime in the disinfection powder encounters the moisture in the medical waste , The reaction generates heat, which promotes the sterilization of germs in medical waste. At the same time, after medical waste is compressed into fuel blocks, during the combustion process, lime can absorb part of the hydrogen chloride in the combustion exhaust gas, thereby reducing the pressure of exhaust gas disposal. The incorporation of fly ash, on the one hand, acts as a barrier, and on the other hand, the fly ash contains a large number of glass beads, which have a lubricating effect, thereby preventing medical waste from sticking to each other during the crushing and grinding process, and promoting the separation of medical waste and disinfection powder. Mix more evenly. In one embodiment, the specific surface area of quicklime > 300m 2 /kg, and the specific surface area of fly ash > 500m 2 /kg, in order to ensure sufficient disinfection, the storage time in the
消毒粉中生石灰通过反应生热,促进了医疗废物中的病菌消杀,在后期形成的燃料燃烧时能够净化废气中的氯化氢,从而减轻废气处置压力。粉煤灰中含有大量玻璃微珠,具有润滑作用,从而避免医疗废物在破碎粉磨过程中相互粘连,促使医疗废物与消毒粉更均匀混合。The quicklime in the disinfection powder generates heat through the reaction, which promotes the sterilization of germs in the medical waste. When the fuel formed in the later stage is burned, it can purify the hydrogen chloride in the waste gas, thereby reducing the pressure of waste gas disposal. Fly ash contains a large number of glass microspheres, which have a lubricating effect, thereby preventing medical waste from sticking to each other during the crushing and grinding process, and promoting a more uniform mixing of medical waste and disinfection powder.
在另一可选实施例中,步骤S5粘合剂包括以下组份的原料,羟丙基甲基纤维素的重量份数为0.02~0.1份,工业预糊化淀粉的重量份数为1~3份、硼砂的重量份数为0.05~0.2份,造纸黑液的重量份数为2~10份;粘合剂的加入有利于破碎产品的后期成型,上述粘合剂在烘干后均具有一定燃烧热值,能够提高成型后燃料棒的燃烧热值,通过粘合剂与挤压成型相结合,能够使产品更易于成型,便于运输和燃烧。在本实施例中,羟丙基甲基纤维素可以为0.02重量份数、0.05重量份数、0.08重量份数或者0.1重量份数,工业预糊化淀粉可以为1重量份数、1.5重量份数、2重量份数、2.5重量份数或者3 重量份数、硼砂可以为0.05重量份数、0.08重量份数、0.1重量份数、0.15 重量份数或者0.2重量份数,造纸黑液可以为2重量份数、3重量份数、5重量份数、8重量份数、9重量份数或者10重量份数,在一个实施例中,优选粘合剂包括羟丙基甲基纤维素的重量份数为0.1份,工业预糊化淀粉的重量份数为3份、硼砂的重量份数为0.2份,造纸黑液的重量份数为10份。In another optional embodiment, the adhesive in step S5 includes raw materials of the following components, the parts by weight of hydroxypropyl methylcellulose are 0.02-0.1 parts by weight, and the parts by weight of industrial pregelatinized starch are 1-2 parts by weight 3 parts, the parts by weight of borax are 0.05~0.2 parts, and the parts by weight of papermaking black liquor are 2~10 parts; A certain combustion calorific value can increase the combustion calorific value of the formed fuel rod, and the combination of adhesive and extrusion molding can make the product easier to form, convenient for transportation and combustion. In this embodiment, hydroxypropyl methylcellulose can be 0.02 parts by weight, 0.05 parts by weight, 0.08 parts by weight or 0.1 parts by weight, and industrial pregelatinized starch can be 1 part by weight, 1.5 parts by weight number, 2 parts by weight, 2.5 parts by weight or 3 parts by weight, borax can be 0.05 parts by weight, 0.08 parts by weight, 0.1 parts by weight, 0.15 parts by weight or 0.2 parts by weight, and the papermaking black liquor can be 2 parts by weight, 3 parts by weight, 5 parts by weight, 8 parts by weight, 9 parts by weight or 10 parts by weight, in one embodiment, the preferred binder comprises the weight of hydroxypropyl methylcellulose The parts are 0.1 parts, the parts by weight of industrial pregelatinized starch are 3 parts, the parts by weight of borax are 0.2 parts, and the parts by weight of papermaking black liquor are 10 parts.
在一实施例中,工业预糊化淀粉的水分含量<9%,灰分<0.5%,糊化度>55%;羟丙基甲基纤维素粘度为100000~200000mPa·s;硼砂中四硼酸钠含量>95%;造纸黑液中木质素和半纤维素浓度为25%~60%(例如25%、 35%、40%、50%、60%),造纸废液粘度<1000mPa·s。In one embodiment, the moisture content of the industrial pregelatinized starch is <9%, the ash content is <0.5%, and the degree of gelatinization is >55%; the viscosity of hydroxypropyl methylcellulose is 100000-200000mPa·s; The content is >95%; the concentration of lignin and hemicellulose in papermaking black liquor is 25% to 60% (eg 25%, 35%, 40%, 50%, 60%), and the viscosity of papermaking waste liquor is <1000mPa·s.
在另一可选实施例中,在医疗废物挤压成型前,先加入按照比例混合后的羟丙基甲基纤维素、工业预糊化淀粉、硼砂,然后以60~100r/min转速对粘合剂和医疗废物进行搅拌混合,搅拌时间为1~20min,通过搅拌使粘合剂和医疗废物充分混合,最后将造纸黑液喷洒至医疗废物上,继续搅拌1~ 10min,造纸黑液通过高压喷嘴喷洒在医疗废物上,能够保证粘合剂和医疗废物混合均匀。In another optional embodiment, before the medical waste is extruded, hydroxypropyl methylcellulose, industrial pregelatinized starch, and borax mixed according to the proportion are added first, and then the viscose is mixed at a speed of 60-100r/min. The mixture and medical waste are stirred and mixed, the stirring time is 1-20min, the adhesive and medical waste are fully mixed by stirring, and finally the paper-making black liquor is sprayed on the medical waste, and the stirring is continued for 1-10min, and the paper-making black liquor passes through the high pressure The nozzle sprays on the medical waste, which can ensure that the adhesive and the medical waste are evenly mixed.
在另一可选实施例中,步骤S6,医疗废物通过成型设备4成型,成型温度为10~40℃,成型设备4可以为压块机,通过挤压成型,将医疗废物成型为圆柱形或棱柱形,横截面积为1~64cm2,长度为2~20cm,优选的,在成型过程中对医疗废物进行保压,保持成型压力为2MPa~20MPa,具体可以为2MPa、11MPa、20MPa等,保压时间5~25s,具体可以为5s、15s、25s等,保证成型后的医疗废物具有较高的强度性能;微波烘干所采用的微波功率>10KW,烘干时间为10s~1800s,具体烘干时间视成品燃料棒的含水量而定,具体可以为10s、30s、60s、1200s、1800s等,在此不对烘干时间进行限定,以使烘干后燃料棒含水率<10%为准,微波烘干效率高、速度快,并先从核心发热,逐步辐射外围,烘干效果良好,烘干后的燃料块热值可进一步提高。In another optional embodiment, in step S6, the medical waste is formed by the forming equipment 4 at a temperature of 10-40°C. The forming equipment 4 can be a briquetting machine, and the medical waste is formed into a cylindrical or Prismatic, with a cross-sectional area of 1-64cm 2 and a length of 2-20cm. Preferably, the medical waste is kept under pressure during the molding process, and the molding pressure is kept at 2MPa-20MPa, specifically 2MPa, 11MPa, 20MPa, etc. The pressure holding time is 5-25s, specifically 5s, 15s, 25s, etc., to ensure that the formed medical waste has high strength performance; the microwave power used in microwave drying is > 10KW, and the drying time is 10s-1800s. The drying time depends on the moisture content of the finished fuel rod, which can be 10s, 30s, 60s, 1200s, 1800s, etc. The drying time is not limited here, so that the moisture content of the fuel rod after drying is <10%. , Microwave drying has high efficiency and fast speed, and heats up from the core first, and gradually radiates to the periphery. The drying effect is good, and the calorific value of the dried fuel block can be further improved.
对本发明实施例所制备的医疗废物燃料块进行性能测试,延展率和耐性指数是评价燃料块堆放储存和长距离运输的关键指标,其中延展率计算公式为:延展率=(10天燃料块长度-燃料块原始长度)/燃料块原始长度,耐性指数计算公式:耐性指数=燃料块跌落残片质量/燃料块总质量,其中跌落高度为2m,跌落次数为10次。性能测试结果如下表所示:Carry out performance tests on the medical waste fuel block prepared by the embodiment of the present invention, the elongation rate and the tolerance index are key indicators for evaluating fuel block stacking storage and long-distance transportation, wherein the elongation rate calculation formula is: elongation rate=(10-day fuel block length -The original length of the fuel block)/the original length of the fuel block, the resistance index calculation formula: resistance index=mass of the falling fragments of the fuel block/total mass of the fuel block, where the drop height is 2m and the number of drops is 10 times. The performance test results are shown in the table below:
在另一可选实施例中,通过抽风机13对医废处理设备产生的废气导向空气净化装置15,进行废气消毒处理,对医疗废物中含有的有害成分进行集中净化,避免溢出。空气净化装置15至少包括布袋除尘器、UV光催化氧化装置和活性炭吸附装置,其中布带除尘器用于出去废气中的颗粒状物体,UV 光催化氧化装置能够快速杀灭废气中含有的残余病菌,活性炭吸附装置能够进一步吸附废气中的异味,由此所使生产中所排向大气的空气是无菌的、洁净的。In another optional embodiment, the waste gas generated by the medical waste treatment equipment is guided to the
在本实施中,双级双轴撕碎机1、研磨粉碎设备3、缓存装置2、搅拌设备10、微波烘干设备5、挤压成型设备4和打包设备6对应设置在封闭仓11 内,通过封闭仓11实现生产线密封,避免医疗垃圾中含有传染性气体溢出,抽风机13分别通过抽风管道将封闭仓11内的废气导向空气净化装置15,抽风管道包括多个支管12,多个支管12分别伸入封闭仓11并延伸至对应的设备,所述空气净化装置15与抽风机13的出气端之间设有冷凝器14,将废气进行冷却。In this implementation, the two-stage two-shaft shredder 1, the grinding and crushing equipment 3, the
在另一可选实施例中,磁选装置7的磁感应强度为800mT-1000mT,磁选装置7可以为永磁滚筒磁选机或者带式磁选机。In another optional embodiment, the magnetic induction of the
在另一可选实施例中,双级双轴撕碎机1包括:进料仓101,进料仓101 上方为方形,进料仓101侧部设置进料仓进料口,在进料仓进料口处设置闸板102,闸板102通过驱动装置驱动,在进料仓进料口设有感应装置,感应装置和驱动装置对应连接在控制器上;进料仓101通过提升装置8进行医疗废物上料,感应装置检测到医疗废物提升至进料仓进料口时,通过控制器控制闸板102打开,在进行垃圾粉碎时,闸板102关闭后以对进料仓进料口进行密封,避免垃圾破碎过程中所产生的废气溢出,感应装置可以为红外感应器,控制器可以为plc或者单片机,驱动装置可以为撕碎电机103。In another optional embodiment, the two-stage twin-shaft shredder 1 includes: a
在进料仓101的底部设置破碎机构,两个破碎机构沿纵向间隔分布在进料仓101下方,两个破碎机构之间通过导料嘴104连通,位于上方的破碎机构对应连通进料仓101下端,医疗废物自进料仓101进入位于上方的破碎机构,经过一次破碎后通过导料嘴104进入下方的破碎机构中,通过两个破碎机构的破碎提高了破碎效率,每个破碎机构包括刀箱106和主轴108,刀箱 106为方形,两个主轴108平行分布在刀箱106内,主轴108的两端通过轴承转动连接刀箱106,并伸出刀箱106外部,主轴108伸出刀箱106之后对应连接有撕碎电机,通过两个撕碎电机分别带动两个主轴108相对转动,使位于两个主轴108上方的医疗废物导向主轴108下方,其中,每个主轴108 上均设有多个动刀107,两个主轴108上的动刀107交错设置;同一主轴108 上,任意相邻两个动刀107之间均设有耐磨盘110,动刀107外缘与耐磨盘 110外缘相切,在主轴108进行转动的同时,一个主轴108上的动刀107将垃圾挤压在另一个主轴108的耐磨盘110上,从而通过挤压撕碎医疗废物,在刀箱106的两侧设有对应耐磨盘110的定刀109,定刀109内侧免倾斜延伸至刀箱106内壁的上沿,以形成对应两个主轴108的斜坡,对医疗废物进行导向;在动刀107周向均匀分布有多个刀刃,相邻两个动刀107之间的刀刃错位设置,刀刃为对应主轴108转动方向的棘齿状,能够提高动刀107驱动垃圾的能力,刀片本体上布设有3~6个刀刃,相邻两刀片单元上的刀刃错位角度为5°~10°。导料嘴104上设有投放口105,用于投放消毒粉,在下方的破碎机构破碎同时对将医疗废物与消毒粉进行混合。A crushing mechanism is set at the bottom of the
在另一可选实施例中,研磨粉碎设备3包括研磨电机301和外壳305,研磨电机301连接减速机302,减速机302连接研磨螺旋304,研磨螺旋304 边缘设有螺旋研磨齿,研磨螺旋304伸入外壳305内,外壳305内腔与研磨螺旋304相适配,在外壳305上设有进料口303、出料口、检修口,进料口 303位于外壳305对应研磨电机301的一端,出料口设置于外壳305的另一端,在外壳305内壁设有外壳研磨齿309,螺旋研磨齿与外壳研磨齿309互嵌并留有间隙,螺旋研磨齿与外壳研磨齿309之间的间隙为5~10mm,在研磨螺旋304输送医疗垃圾的同时通过螺旋研磨齿308与外壳研磨齿309进行研磨,使医疗垃圾充分破碎。检修口可以为多个,均匀分布在外壳305上,便于进行检修。螺旋研磨齿为条形,螺旋研磨齿沿研磨螺旋304长度方向连接在其边缘,外壳研磨齿309为条形并与螺旋研磨齿相适配,随着研磨螺旋 304的转动螺旋研磨齿与外壳研磨齿309相互交错,在交错过程中对医疗垃圾进行研磨。In another optional embodiment, the grinding and crushing equipment 3 includes a grinding
在另一可选实施例中,缓存装置2的主体为料塔,料塔内部设有料位监测模块206、温度检测模块203和pH检测模块204,在料塔下方设置有重量检测装置205,能够实时监测医疗废物的状态,料塔的底部设有对应连接输料器的出口,在料塔外壁设有夹层201,料塔内腔设有多组在纵向上均匀分布的换热管202,换热管202的两端穿过料塔对应连通夹层201,夹层201 上设有进液口和出液口,向夹层201内循环供入热介质,热介质可以为导热油或者蒸汽,以对医废进行加热,从而提高医疗废物的消毒效果,在本实施例中,热介质的温度为115℃。在料塔的出口处设有风嘴207,风嘴207有多个,多个风嘴207设置于料塔出口处的内壁下沿,并指向料塔内部,风嘴207 对应连接热风装置,用于向料塔内供入热风,热风温度可以为100-105℃,能够辅助进行消毒,同时,通过风嘴207吹风可使料塔中的医疗废物处于局部流化状态,使料塔出料更顺畅。可以理解的是,以上描述仅为示例性的,本申请实施例对此并不进行限定。In another optional embodiment, the main body of the
以上所述仅为本发明的较佳实施例而已,并不用以限制本发明,凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均在本发明待批权利要求保护范围之内。The above descriptions are only preferred embodiments of the present invention, and are not intended to limit the present invention. Any modifications, equivalent replacements, improvements, etc. made within the spirit and principles of the present invention are within the scope of the pending rights of the present invention. within the scope of protection.
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Denomination of invention: A method of using medical waste adhesive to compress recycled fuel Granted publication date: 20230623 Pledgee: Zhengzhou Zhongyuan Development Investment (Group) Co.,Ltd. Pledgor: ZHENGZHOU HAN YNAG TIAN CHEN HAZARDOUS WASTE DISPOSAL CO.,LTD.|SHANGQIU TIANCHEN ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd.|Henan Tianchen Xinyuan Environmental Protection Technology Research Institute Co.,Ltd. Registration number: Y2024980021471 |
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