CN103143432B - Efficient crushing and three-section type screening method of coking coal gravity middings - Google Patents
Efficient crushing and three-section type screening method of coking coal gravity middings Download PDFInfo
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Abstract
一种炼焦煤重选中煤的高效破碎和三段式分选方法,属于煤炭破碎解离分选工艺。以炼焦煤选煤厂重选中煤为原料,辊压破碎至6mm或3mm以下;使用脱泥筛对<1mm粒级物料脱泥,6~1mm或3~1mm粒级物料进入三产品重介质旋流器,经两段脱介后分别得到精煤、中煤和矸石;<1mm粒级物料与精煤磁选机尾矿混合后采用分级旋流器组脱出<0.25mm粒级细煤泥;1~0.25mm粒级粗煤泥进入干扰床分选机进行分选,轻产物经弧形筛、煤泥离心机脱水后得到粗精煤,重产物经沉降过滤式离心机脱水后成为尾煤;<0.25mm粒级细煤泥进入浮选机进行浮选,泡沫精煤和尾煤分别经浓缩、压滤脱水后得到浮选精煤和尾煤产品;重选中煤经过辊压破碎后产物返回混料桶。优点:对预选粗、细粒级煤泥分级分选,提高了设备的分选精度。
The invention discloses a high-efficiency crushing and three-stage separation method for heavy separation of coking coal, which belongs to the coal crushing, dissociation and separation process. The coking coal coal preparation plant re-selected coal is used as raw material, and it is crushed to 6mm or below 3mm by roll pressing; the material with a particle size of <1mm is deslimed with a desliming screen, and the material with a particle size of 6~1mm or 3~1mm enters the three-product dense medium cyclone Clean coal, medium coal and gangue are obtained after two-stage deintermediation; <1mm particle size material is mixed with clean coal magnetic separator tailings, and then the graded cyclone group is used to remove <0.25mm particle size fine coal slime; Coarse coal slime with particle size of 1~0.25mm enters the interference bed sorter for separation. The light product is dehydrated by a curved screen and a slime centrifuge to obtain coarse clean coal, and the heavy product is dehydrated by a sedimentation filter centrifuge to become tailing coal. ;<0.25mm particle size fine coal slurry enters the flotation machine for flotation, and the foamed clean coal and tailing coal are respectively concentrated, filtered and dehydrated to obtain the flotation clean coal and tailing coal products; Return to mixing bucket. Advantages: Classification and separation of pre-selected coarse and fine-grained coal slime improves the separation accuracy of the equipment.
Description
技术领域 technical field
本发明涉及一种煤炭破碎解离分选工艺,尤其涉及一种炼焦煤重选中煤的高效破碎和三段式分选方法。 The invention relates to a coal crushing, dissociation and separation process, in particular to a high-efficiency crushing and three-stage separation method for heavy separation of coking coal.
背景技术 Background technique
我国煤炭资源储量丰富,煤种齐全,但炼焦煤资源相对缺乏,约占27.6%。其中肥煤、焦煤和瘦煤三种炼焦煤分别占煤炭总资源量的3.75%、6.71%和4.17%。目前,作为炼焦工业不可缺少的焦煤和肥煤资源已成为稀缺资源,其开采及加工利用已受到国家政策或能源战略的保护,由于多种原因,现有的炼焦用煤中煤的回收工艺对于稀缺资源的回收效率较低,亟需合理高效的炼焦用煤分选回收工艺。 my country has abundant reserves of coal resources and a complete range of coal types, but the resources of coking coal are relatively scarce, accounting for about 27.6%. Among them, fat coal, coking coal and lean coal account for 3.75%, 6.71% and 4.17% of the total coal resources respectively. At present, coking coal and fat coal resources, which are indispensable for the coking industry, have become scarce resources, and their mining, processing and utilization have been protected by national policies or energy strategies. The recovery efficiency of scarce resources is low, and there is an urgent need for a reasonable and efficient separation and recovery process for coking coal.
发明内容 Contents of the invention
本发明的目的是要提供一种炼焦煤重选中煤的高效破碎和三段式分选方法,解决现有的稀缺炼焦用煤回收率低的问题。 The purpose of the present invention is to provide a high-efficiency crushing and three-stage separation method for coking coal gravity separation, so as to solve the problem of low recovery rate of the existing scarce coking coal.
本发明的目的是这样实现的,采用以下技术方案:以炼焦煤选煤厂重选中煤为原料,采用破碎解离、选前脱泥、粗中细粒级三段分选的方法,按照以下步骤进行: The purpose of the present invention is achieved in this way, adopt the following technical scheme: take the re-selected coal of the coking coal preparation plant as raw material, adopt the method of crushing and dissociation, desliming before election, coarse, medium and fine-grained three-stage separation, according to the following Steps to proceed:
(1) 利用除铁器除去重选中煤中的铁器杂物后,进入辊压破碎机1,辊压破碎机1入料粒度<50mm,出料粒度<6mm; (1) Use the iron remover to remove the iron sundries in the gravity-selected coal, and then enter the roller crusher 1, the input particle size of the roller crusher 1 is <50mm, and the output particle size is <6mm;
(2) 利用辊压破碎机1对中煤进行破碎,破碎后的<6mm粒级物料进入脱泥筛,脱泥筛需添加喷淋循环水,循环水量不足时,以清水作为补充; (2) Use the roller crusher 1 to crush the medium coal, and the crushed materials with a particle size of <6mm enter the desliming screen. The desliming screen needs to be added with spray circulating water. When the circulating water is insufficient, clean water is used as a supplement;
(3) 利用筛孔为1mm的脱泥筛湿法脱除入料中<1mm的煤泥,6~1mm粒级筛上物进入混料桶; (3) Use a desliming sieve with a sieve hole of 1mm to remove the coal slime <1mm in the feed by wet method, and the sieve with a size of 6~1mm enters the mixing tank;
(4) 在混料桶中,6~1mm粒级脱泥筛筛上物与辊压破碎机2返回破碎物料混合后,用泵打至三产品重介质旋流器进行分选,三产品重介质旋流器为两段式等密度重介质旋流器,一段进行旋流力场分选,二段进行强旋流精选; (4) In the mixing tank, after the 6~1mm particle size desilting sieve supernatant is mixed with the crushed material returned by the roller crusher 2, it is pumped to the three-product heavy medium cyclone for sorting, and the three-product heavy medium cyclone is sorted. The medium cyclone is a two-stage equal-density dense medium cyclone, one stage is for swirling force field sorting, and the second stage is for strong swirling flow selection;
(5) 混料桶中的混合物料与合格介质的混合物在三产品重介质旋流器的旋流分选作用下,轻产物进入精煤脱介筛,中间产物进入中煤脱介筛,重产物进入矸石脱介筛,精煤脱介筛、中煤脱介筛和矸石脱介筛需添加喷淋循环水,循环水量不足时,以清水作为补充; (5) The mixture of the mixed material and the qualified medium in the mixing tank is under the cyclone separation of the three-product heavy medium cyclone, the light product enters the clean coal de-mediation sieve, the intermediate product enters the medium coal de-medium sieve, and the heavy The product enters the gangue removal sieve, and the clean coal removal sieve, the medium coal removal sieve and the gangue removal sieve need to add spray circulating water. When the amount of circulating water is insufficient, clean water is used as a supplement;
(6) 精煤脱介筛一段脱出浓介质,二段脱出稀介质,筛上物成为重介精煤产品;利用精煤磁选机对稀介质进行磁选,磁选精矿与一段脱出的浓介质一同进入合格介质桶; (6) The first stage of the clean coal removal screen removes the dense medium, and the second stage removes the thin medium, and the sieve becomes a dense medium clean coal product; the clean coal magnetic separator is used to magnetically separate the thin medium, and the magnetic separation concentrate is separated from the first stage. Thick medium enters the qualified medium barrel together;
(7) 中煤脱介筛一段脱出浓介质,二段脱出稀介质,筛上物进入辊压破碎机2;中煤脱介筛一段脱出的浓介质进入合格介质桶,二段脱出的稀介质进入中矸磁选机; (7) The first stage of medium coal de-mediation sieve removes the dense medium, the second stage removes the thin medium, and the oversize enters the roller crusher 2; Enter the middle gangue magnetic separator;
(8) 矸石脱介筛一段脱出浓介质,二段脱出稀介质,筛上物成为矸石产品;矸石脱介筛一段脱出的浓介质进入合格介质桶,二段脱出的稀介质与中煤脱介筛二段脱出的稀介质一同进入中矸磁选机,利用中矸磁选机对稀介质进行磁选,磁选精矿进入合格介质桶,合格介质桶的合格介质用泵打至三产品重介质旋流器作为分选介质,通过补加介质或补加清水的方法调节合格介质桶的介质密度; (8) The first stage of the gangue removal sieve removes the dense medium, the second stage removes the thin medium, and the sieve becomes gangue products; The dilute medium extracted from the second section of the sieve enters the medium gangue magnetic separator together, and the medium gangue magnetic separator is used to magnetically separate the dilute medium, and the magnetic separation concentrate enters the qualified medium barrel, and the qualified medium in the qualified medium barrel is pumped to the third product The medium cyclone is used as the sorting medium, and the medium density of the qualified medium barrel is adjusted by adding medium or adding clean water;
(9) 在辊压破碎机2的辊压破碎作用下,中煤脱介筛筛上物被破碎为小块,返回混料桶; (9) Under the action of the roller crushing of the roller crusher 2, the material on the medium coal de-mediation sieve is broken into small pieces and returned to the mixing tank;
(10) 脱泥筛筛下物与精煤磁选尾矿在煤泥桶中混合后,用泵打至分级旋流器组进行分级,分级旋流器组溢流进入调浆桶,底流进入干扰床分选机;所述的溢流的粒度为<0.25mm粒级细煤泥;所述的底流粒度为1~0.25mm粒级粗煤泥; (10) After mixing the undersize of the desliming screen and the clean coal magnetic separation tailings in the slime tank, pump it to the grading cyclone group for grading. The overflow of the grading cyclone group enters the slurry tank, and the underflow enters the Interference bed separator; the particle size of the overflow is <0.25mm fine coal slime; the underflow particle size is 1~0.25mm coarse coal slime;
(11) 在干扰床分选机的分选作用下,轻产物进入精煤弧形筛,重产物进入沉降过滤式离心机,干扰床分选机需要循环水/清水作为顶水,当循环水池中的水量不足时,以清水作为补充; (11) Under the separation action of the disturbed bed separator, the light products enter the clean coal arc screen, and the heavy products enter the sedimentation filter centrifuge. The disturbed bed separator needs circulating water/clean water as the top water. When the circulating water tank When the water in the container is insufficient, supplement it with clean water;
(12) 使用精煤弧形筛对干扰床分选机轻产物进行一次脱水,筛上物进入精煤离心机,筛下物进入调浆桶; (12) Use the clean coal curved screen to dehydrate the light product of the disturbed bed separator once, the oversize material enters the clean coal centrifuge, and the undersize material enters the slurry mixing tank;
(13) 使用精煤离心机对精煤弧形筛筛上物进行二次脱水,其产品即为粗精煤,离心液与精煤弧形筛筛下物一起进入调浆桶; (13) Use a clean coal centrifuge to dehydrate the material on the clean coal arc screen for a second time, and the product is coarse clean coal, and the centrifugal liquid enters the slurry mixing tank together with the under matter of the clean coal arc screen;
(14) 使用沉降过滤式离心机对干扰床分选机重产物进行脱水,其产品即为尾煤,滤液进入尾煤浓缩机; (14) Use a sedimentation filter centrifuge to dehydrate the heavy product of the interference bed separator, and the product is tailing coal, and the filtrate enters the tailing coal thickener;
(15) 分级旋流器组溢流与精煤压滤机返回滤液、精煤弧形筛筛下物及精煤离心机离心液在调浆桶中进行调浆预处理后,进入浮选机分选; (15) After the overflow of the grading cyclone group and the return filtrate of the clean coal filter press, the sieve of the clean coal arc screen and the centrifugate of the clean coal centrifuge are pretreated in the slurry mixing tank, they enter the flotation machine sorting;
(16) 在浮选机分选作用下,浮选机泡沫精煤进入精煤压滤机,尾煤进入尾煤浓缩机; (16) Under the separation action of the flotation machine, the foamed clean coal of the flotation machine enters the clean coal filter press, and the tailing coal enters the tailing coal thickener;
(17) 使用精煤压滤机对浮选机精煤进行脱水,脱水后产品即为浮选精煤产品,滤液返回调浆桶; (17) Use the clean coal filter press to dehydrate the clean coal of the flotation machine. The product after dehydration is the flotation clean coal product, and the filtrate is returned to the slurry tank;
(18) 中矸磁选尾矿、浮选机尾煤与沉降过滤式离心机离心液一同进入尾煤浓缩机,浓缩机溢流进入循环水池,底流进入尾煤压滤机; (18) The tailings of the medium gangue magnetic separation, the tailings of the flotation machine and the centrifugal liquid of the sedimentation filter centrifuge enter the tailings thickener together, the overflow of the thickener enters the circulating pool, and the underflow enters the tailings filter press;
(19) 使用尾煤压滤机对尾煤浓缩机底流进行脱水,压滤机产品即为尾煤产品,滤液进入循环水池。 (19) Use the tailing coal filter press to dehydrate the bottom flow of the tailing coal thickener, the product of the filter press is the tailing coal product, and the filtrate enters the circulating pool.
有益效果:由于采用了上述方案,对稀缺炼焦煤重选中煤采用了两次破碎-粗中细粒级分别进行重介分选、干扰床分选和浮选三段分选工艺方法,有效实现了“分步释放、逐级回收”。将重选中煤破碎至<6mm粒级,使块煤与矿物质连生体发生解离,6~1mm粒级原煤采用技术成熟的三产品重介质旋流器,即两段式等密度重介质旋流器进行分选,提高了粗粒级的分选精度;<1mm粒级煤泥采用分级旋流器组分级后,1~0.25mm粒级粗煤泥采用干扰床分选机分选,<0.25mm粒级细煤泥采用浮选机分选,三产品重介质旋流器中煤产品采用辊压破碎机进行二次破碎,使粗粒中煤中的煤与矿物质连生体进一步解离,大大提高了粗细粒煤泥的分选精度和回收率。 Beneficial effects: Due to the adoption of the above-mentioned scheme, two crushing-coarse, medium and fine-grained grades are respectively used for dense medium separation, disturbed bed separation and flotation three-stage separation process for the rare coking coal heavy separation coal, effectively realizing "Step-by-step release, step-by-step recycling". Crush the gravity-selected coal to a particle size of <6mm to dissociate the lump coal and the mineral intergrowth. The raw coal with a particle size of 6-1mm adopts a three-product dense medium cyclone with mature technology, that is, a two-stage isodensity dense medium cyclone Sorting with a flow device improves the separation accuracy of the coarse-grained class; after the <1mm particle size coal slime is classified by the classifying cyclone group, the 1-0.25mm particle size coarse coal slime is separated by an interference bed sorter, < The 0.25mm fine coal slime is sorted by flotation machine, and the coal product in the three-product dense medium cyclone is crushed by roller crusher for secondary crushing, so that the coal and minerals in the coarse coal can be further dissociated. , greatly improving the separation accuracy and recovery rate of coarse and fine coal slime.
优点:重选中煤经破碎解离后,采用重介分选、干扰床分选和浮选三段分选工艺,预选脱出的粗、细粒级煤泥分级分选,提高了设备的分选精度,并尽可能地回收稀缺炼焦煤炭资源,增加经济、社会和生态效益。 Advantages: after crushing and dissociation of the gravity-selected coal, the three-stage separation process of dense medium separation, disturbed bed separation and flotation is used to pre-select and separate the coarse and fine-grained coal slime, which improves the separation efficiency of the equipment. Accuracy, and recover scarce coking coal resources as much as possible, increase economic, social and ecological benefits.
附图说明 Description of drawings
图1是本发明实施的工艺流程图。 Fig. 1 is a process flow chart of the present invention's implementation.
具体实施方式 Detailed ways
实施例1:图1中,稀缺炼焦煤重选中煤通过胶带输送机机头附近的除铁器,除去铁器杂物,进入辊压破碎机1,破碎产物进入筛孔为1mm的湿法脱泥筛,湿法脱泥筛筛上物与辊压破碎机2返回料混合后,用泵打至三产品重介质旋流器,轻产物进入精煤脱介筛,一段脱出的浓介质进入合格介质桶,二段脱出的稀介质进入精煤磁选机,磁选精矿进入合格介质桶,尾矿进入煤泥桶,筛上物即为重介精煤产品;三产品重介质旋流器的中间产物进入中煤脱介筛,一段脱出的浓介质进入合格介质桶,二段脱出的稀介质进入中矸磁选机,磁选精矿进入合格介质桶,尾矿进入尾煤浓缩机,筛上物进入辊压破碎机2;三产品重介质旋流器的重产物进入矸石脱介筛,一段脱出的浓介质进入合格介质桶,二段脱出的稀介质进入中矸磁选机,磁选精矿进入合格介质桶,尾矿进入尾煤浓缩机,筛上物即为矸石产品;脱泥筛筛下物在煤泥桶中与精煤磁选机尾矿混合后,用泵打至分级旋流器组,溢流进入调浆桶,底流进入干扰床分选机,干扰床分选机轻产物进入精煤弧形筛,精煤弧形筛筛上物进入精煤离心机,精煤离心机产品即为粗精煤产品,离心液与精煤弧形筛筛下物混合进入调浆桶;干扰床分选机重产物进入沉降过滤式离心机,离心机产品即为尾煤产品,离心液进入尾煤浓缩机;分级旋流器组溢流与精煤压滤机返回滤液、精煤弧形筛筛下物及精煤离心机离心液混合进入调浆桶,经调浆预处理后进入浮选机,浮选机泡沫产品进入精煤压滤机,压滤机产品即为浮选精煤产品,滤液返回调浆桶;浮选机尾煤进入尾煤浓缩机,尾煤浓缩机溢流进入循环水池,尾煤浓缩机底流进入尾煤压滤机,尾煤压滤机滤液进入循环水池,尾煤压滤机产品即为尾煤产品。 Embodiment 1: In Fig. 1, the rare coking coal re-selected coal passes through the iron remover near the head of the belt conveyor to remove iron debris, enters the roller crusher 1, and the crushed product enters the wet desliming screen with a sieve hole of 1mm , after the material on the wet desliming sieve is mixed with the return material of the roller crusher 2, it is pumped to the three-product heavy medium cyclone, the light product enters the clean coal de-medium sieve, and the concentrated medium extracted from a section enters the qualified medium barrel , the dilute medium extracted from the second stage enters the clean coal magnetic separator, the magnetically separated concentrate enters the qualified medium barrel, the tailings enter the slime barrel, and the screened material is the dense medium clean coal product; the middle of the third product dense medium cyclone The product enters the medium coal removal sieve, the concentrated medium extracted from the first stage enters the qualified medium barrel, the dilute medium extracted from the second stage enters the medium gangue magnetic separator, the magnetic separation concentrate enters the qualified medium barrel, and the tailings enter the tailings thickener. The material enters the roller crusher 2; the heavy product of the three-product heavy medium cyclone enters the gangue removal screen, the dense medium extracted from the first stage enters the qualified medium barrel, and the thin medium extracted from the second stage enters the medium gangue magnetic separator, and the magnetic separation fine The ore enters the qualified medium barrel, the tailings enter the tailings thickener, and the screened material is the gangue product; the screened material of the desliming screen is mixed with the tailings of the clean coal magnetic separator in the slime tank, and then pumped to the classification rotary Flow device group, the overflow enters the slurry tank, the underflow enters the interference bed separator, the light product of the interference bed separator enters the clean coal arc screen, the clean coal arc screen screen enters the clean coal centrifuge, and the clean coal centrifuge The product of the centrifuge is the coarse clean coal product, and the centrifugal liquid is mixed with the undercut of the clean coal arc screen into the slurry mixing tank; the heavy product of the disturbance bed separator enters the sedimentation filter centrifuge, and the product of the centrifuge is the tailing coal product. The liquid enters the tailing coal thickener; the overflow of the grading cyclone group is mixed with the return filtrate of the clean coal filter press, the sieve of the clean coal arc sieve and the centrifuge liquid of the clean coal centrifuge and enters the slurry mixing barrel, and after slurry pretreatment Enter the flotation machine, the foam product of the flotation machine enters the clean coal filter press, the product of the filter press is the flotation clean coal product, and the filtrate returns to the slurry tank; the tailing coal of the flotation machine enters the tailing coal thickener, and the tailing coal thickener The overflow enters the circulating pool, the underflow of the tailing coal thickener enters the tailing coal filter press, and the filtrate of the tailing coal filter press enters the circulating pool, and the product of the tailing coal filter press is the tailing coal product.
在脱泥和脱介过程中需加喷淋循环水,干扰床分选机需要循环水/清水作为顶水,当循环水池中的水量不足时,以清水作为补充。精煤、中煤和矸石脱出的浓介质和磁选精矿进入合格介质桶,引起介质密度变化时,可通过补加介质或补加清水的方法进行调整。 In the process of desliming and descaling, spraying circulating water is required. The disturbed bed sorter needs circulating water/clean water as top water. When the water in the circulating pool is insufficient, clean water is used as a supplement. The dense medium and magnetic separation concentrate from clean coal, medium coal and gangue enter the qualified medium barrel, and when the density of the medium changes, it can be adjusted by adding medium or adding water.
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