CN104531171B - A kind of high-efficient energy-saving environment friendly retort - Google Patents
A kind of high-efficient energy-saving environment friendly retort Download PDFInfo
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- 238000003763 carbonization Methods 0.000 claims abstract description 55
- 238000005096 rolling process Methods 0.000 claims abstract description 11
- 239000007789 gas Substances 0.000 claims description 19
- 239000002994 raw material Substances 0.000 claims description 19
- 239000005539 carbonized material Substances 0.000 claims description 15
- 238000007599 discharging Methods 0.000 claims description 13
- 238000000034 method Methods 0.000 claims description 11
- 238000007789 sealing Methods 0.000 claims description 9
- 238000010438 heat treatment Methods 0.000 claims description 8
- 239000000463 material Substances 0.000 claims description 6
- 230000003014 reinforcing effect Effects 0.000 claims description 6
- 239000011449 brick Substances 0.000 claims description 5
- 239000002918 waste heat Substances 0.000 claims description 5
- 238000001035 drying Methods 0.000 claims description 3
- 238000004227 thermal cracking Methods 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 3
- 230000000694 effects Effects 0.000 claims description 2
- 230000005484 gravity Effects 0.000 claims description 2
- 238000011282 treatment Methods 0.000 claims description 2
- 239000011796 hollow space material Substances 0.000 claims 3
- 238000005292 vacuum distillation Methods 0.000 claims 3
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 claims 2
- 239000011248 coating agent Substances 0.000 claims 2
- 238000000576 coating method Methods 0.000 claims 2
- 239000003063 flame retardant Substances 0.000 claims 2
- 238000001816 cooling Methods 0.000 claims 1
- 230000003009 desulfurizing effect Effects 0.000 claims 1
- 238000013021 overheating Methods 0.000 claims 1
- 230000006698 induction Effects 0.000 abstract description 8
- 239000003245 coal Substances 0.000 description 10
- 238000004519 manufacturing process Methods 0.000 description 8
- 238000000197 pyrolysis Methods 0.000 description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 7
- 239000000047 product Substances 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 3
- 230000008901 benefit Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 210000003437 trachea Anatomy 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B1/00—Retorts
- C10B1/10—Rotary retorts
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
- C10B53/04—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of powdered coal
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B57/00—Other carbonising or coking processes; Features of destructive distillation processes in general
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Muffle Furnaces And Rotary Kilns (AREA)
- Coke Industry (AREA)
- Carbon And Carbon Compounds (AREA)
Abstract
本发明公开了一种高效节能环保炭化炉,包括下料机、支架、回转筒体、转动装置及出料装置,所述回转筒体以左高右低的方式倾斜安装在所述支架上,所述转动装置通过滚圈带动所述回转筒体转动,所述回转筒体的左端设置有下料机,右端设置有出料装置,所述回转筒体的中空部分为烟道仓,所述回转筒体的筒壁内侧均匀设置有若干炭化仓,所述下料机底端设置有下料器,所述下料器与所述回转筒体左下部的炭化仓一端连接,所述炭化仓的另一端连接所述出料装置;所述烟道仓通过进气管贯穿所述出料装置的中空部分与混风器连接,所述烟道仓通过出气管贯穿所述下料机的中空部分;所述出料装置的上部设置有引风管,引风管的外端与第一引风机连接。
The invention discloses a high-efficiency, energy-saving and environment-friendly carbonization furnace, which comprises a blanking machine, a bracket, a rotary cylinder, a rotating device and a discharge device. The rotating device drives the rotary cylinder to rotate through the rolling ring. The left end of the rotary cylinder is provided with a feeder, and the right end is provided with a discharge device. The hollow part of the rotary cylinder is a flue chamber. A number of carbonization bins are evenly arranged on the inner side of the cylinder wall of the rotary cylinder, and a feeder is provided at the bottom of the feeder, and the feeder is connected to one end of the carbonization bin at the lower left part of the rotary cylinder, and the carbonization bin The other end of the outlet is connected to the discharge device; the flue chamber passes through the hollow part of the discharge device through the air inlet pipe and is connected with the air mixer, and the flue chamber passes through the hollow part of the blanking machine through the air outlet pipe ; The upper part of the discharge device is provided with an air induction pipe, and the outer end of the air induction pipe is connected with the first air induction fan.
Description
技术领域technical field
本发明涉及一种活性炭制备装置领域,特别涉及一种高效节能环保炭化炉。The invention relates to the field of activated carbon preparation devices, in particular to a high-efficiency, energy-saving and environment-friendly carbonization furnace.
背景技术Background technique
采用内热式炭化炉进行煤的干馏,对原料煤要求较高,只能对50mm-150mm的块煤进行炭化,受原料影响较大。且生产过程中有大量焦油和污水产生,生产出的炭化料含水量高,影响活性炭品质。现在的炭化料制作是一种粗放式的生产,生产出的炭化料品质较低,在炭化过程中由于有空气进入造成燃烧固定碳的现象,既降低了炭化得率又影响了炭化料的品质,同时炭化过程中产生的高温燃气没有充分利用,造成能源的浪费和对环境的影响。炭化时物料释放出的一氧化碳、氢气及烃类如甲烷等既污染空气,也是一种能源的浪费,有的需要建造燃烧室来解决炭化所产生的废气,这从另一方面增加了企业的基建投资。在当前低温干馏行业末煤无法综合利用、产品质量不够理想、环保问题尚未根本解决的背景下,亟待将一种适用范围广、可靠稳定的设备推向整个低变质煤综合利用行业,在低变质煤产区投资外热式回转低温干馏系统可以促进企业取得颇丰的经济效益,为企业资源综合利用开辟了全新的途径。The dry distillation of coal in an internal heating carbonization furnace has high requirements for raw coal, and can only carbonize lump coal of 50mm-150mm, which is greatly affected by raw materials. Moreover, a large amount of tar and sewage are produced during the production process, and the carbonized material produced has a high water content, which affects the quality of activated carbon. The current production of carbonized material is an extensive production, and the quality of the produced carbonized material is low. During the carbonization process, the phenomenon of burning and fixing carbon due to the entry of air not only reduces the carbonization yield but also affects the quality of the carbonized material. , At the same time, the high-temperature gas generated in the carbonization process is not fully utilized, resulting in waste of energy and impact on the environment. The carbon monoxide, hydrogen and hydrocarbons such as methane released by materials during carbonization not only pollute the air, but also waste energy. Some need to build combustion chambers to solve the waste gas generated by carbonization, which increases the infrastructure of enterprises on the other hand. invest. Under the background that the fine coal in the low-temperature carbonization industry cannot be comprehensively utilized, the product quality is not satisfactory, and the environmental protection problem has not been fundamentally resolved, it is urgent to promote a reliable and stable equipment with a wide application range to the comprehensive utilization industry of low-metamorphism coal. Investing in an externally heated rotary low-temperature retort system in coal production areas can promote enterprises to obtain considerable economic benefits and open up a new way for enterprises to comprehensively utilize resources.
发明内容Contents of the invention
本发明的目的在于提供一种可循环利用热源的高效节能环保炭化炉。此炭化炉操作简便,可连续生产,节省能源,生产的炭化料产品质量稳定。The object of the present invention is to provide a high-efficiency, energy-saving and environment-friendly carbonization furnace capable of recycling heat sources. The carbonization furnace is easy to operate, can be produced continuously, saves energy, and the quality of the carbonized material produced is stable.
为实现上述目的,本发明提供的高效节能环保炭化炉,包括下料机、支架、回转筒体、转动装置及出料装置,所述回转筒体以左高右低的方式倾斜安装在所述支架上,所述转动装置通过滚圈带动所述回转筒体转动,所述回转筒体的左端设置有下料机,右端设置有出料装置,所述回转筒体的筒壁内侧均匀设置有若干炭化仓,所述回转筒体的中空部分为烟道仓;所述下料机底端设置有下料器,所述下料器与所述回转筒体左下部的炭化仓一端连接,所述炭化仓的另一端连接所述出料装置;所述烟道仓通过进气管贯穿所述出料装置的中空部分与混风器连接,所述烟道仓通过出气管贯穿所述下料机的中空部分;所述出料装置的上部设置有引风管,引风管的外端与第一引风机连接。In order to achieve the above purpose, the high-efficiency, energy-saving and environment-friendly carbonization furnace provided by the present invention includes a blanking machine, a bracket, a rotary cylinder, a rotating device and a discharge device. The rotary cylinder is installed on the On the bracket, the rotating device drives the rotary cylinder to rotate through the rolling ring. The left end of the rotary cylinder is provided with a feeder, and the right end is provided with a discharge device. The inner side of the rotary cylinder is evenly provided with Several carbonization chambers, the hollow part of the rotary cylinder is a flue chamber; the bottom of the feeder is provided with a feeder, and the feeder is connected to one end of the carbonization chamber at the lower left part of the rotary cylinder. The other end of the carbonization bin is connected to the discharge device; the flue bin passes through the hollow part of the discharge device through the air inlet pipe and is connected with the air mixer, and the flue bin passes through the feeder through the outlet pipe The hollow part; the upper part of the discharge device is provided with an air induction pipe, and the outer end of the air induction pipe is connected with the first induced draft fan.
其中,优选的,在所述烟道仓内设置有若干加强筋,用于支撑固定所述炭化仓,保证炭化仓的热胀冷缩自由滑动。Wherein, preferably, several reinforcing ribs are provided in the flue chamber for supporting and fixing the carbonization chamber, so as to ensure the free sliding of the carbonization chamber when it expands with heat and contracts with cold.
优选的,所述烟道仓和所述下料机之间设置有第一密封装置。Preferably, a first sealing device is provided between the flue bin and the feeder.
优选的,所述烟道仓和所述出料装置之间设置第二密封装置。Preferably, a second sealing device is provided between the flue bin and the discharge device.
优选的,所述出料装置的底部设置有冷却器。Preferably, a cooler is provided at the bottom of the discharge device.
优选的,所述混风器内近出料装置端设置有第二引风机,远离出料装置端设置有燃烧器。Preferably, a second induced draft fan is provided in the air mixer near the end of the discharge device, and a burner is provided at the end far away from the discharge device.
优选的,所述回转筒体的内壁设置有耐火层,更优选为耐火砖层。Preferably, the inner wall of the rotating cylinder is provided with a refractory layer, more preferably a refractory brick layer.
优选的,所述滚圈与所述回转筒体之间设置有滚圈垫板。Preferably, a rolling ring backing plate is provided between the rolling ring and the rotating cylinder.
与现有技术相比,本发明具有的优点:Compared with prior art, the present invention has the advantage:
①原料适用范围广:根据产品最终用途,本发明的高效节能环保炭化炉可以处理50mm以下的原煤,包括5mm以下末煤。原料煤粉末充足,抗风险能力强。①Wide range of application of raw materials: According to the final use of the product, the high-efficiency, energy-saving and environmentally-friendly carbonization furnace of the present invention can process raw coal below 50mm, including fine coal below 5mm. The raw coal powder is sufficient, and the ability to resist risks is strong.
②本发明装置操作灵活、弹性大,可根据不同的市场要求即时调整工艺参数改变产品品质。原料煤在炭化仓内经过热处理、低温干馏、热裂解生产炭化料,不和空气接触,杜绝了固定碳的燃烧,有利于生产出得率高、品质好的炭化料。② The device of the present invention has flexible operation and high flexibility, and can adjust process parameters in real time to change product quality according to different market requirements. The raw coal undergoes heat treatment, low-temperature dry distillation, and pyrolysis in the carbonization bin to produce carbonized materials without contact with air, which prevents the combustion of fixed carbon and is conducive to the production of high-yield and high-quality carbonized materials.
③本发明的高效节能环保炭化炉,由于采用余热利用技术,既可以有效地控制各段的温度,又可以杜绝高温气体内的杂质进入炭化料内,有利于生产出高品质的炭化料。由于高温余热的循环利用,节约能源,减少了有害气体及工业污水的生成,减少了相应的治理装置及费用。③The high-efficiency, energy-saving and environment-friendly carbonization furnace of the present invention can not only effectively control the temperature of each section, but also prevent impurities in the high-temperature gas from entering the carbonization material due to the use of waste heat utilization technology, which is conducive to the production of high-quality carbonization materials. Due to the recycling of high-temperature waste heat, energy is saved, the generation of harmful gases and industrial sewage is reduced, and the corresponding treatment devices and costs are reduced.
④装置产能大,年产量大于直立炉。加工成本低,是传统内热式炭化炉的50%。④The production capacity of the device is large, and the annual output is larger than that of the vertical furnace. The processing cost is low, which is 50% of the traditional internal heating carbonization furnace.
附图说明Description of drawings
下面结合附图对本发明作进一步说明:The present invention will be further described below in conjunction with accompanying drawing:
图1为本发明的整体结构示意图;Fig. 1 is the overall structure schematic diagram of the present invention;
图2为本发明A-A剖视图;Fig. 2 is A-A sectional view of the present invention;
图3为本发明B-B剖视图;Fig. 3 is B-B sectional view of the present invention;
图4为本发明C-C剖视图。Fig. 4 is a C-C sectional view of the present invention.
图中:1、下料机,2、支架,3、回转筒体,4、转动装置,5、出料装置,6、烟道仓,7、炭化仓,8、下料器,9、进气管,10、出气管,11、引风管,12、第一引风机,13、加强筋,14、第一密封装置,15、第二密封装置,16、冷却器,17、第二引风机,18、燃烧器,19、耐火砖层,20混风器。In the figure: 1. Feeding machine, 2. Bracket, 3. Rotary cylinder, 4. Rotating device, 5. Discharging device, 6. Flue chamber, 7. Carbonization chamber, 8. Feeder, 9. Inlet Trachea, 10, air outlet pipe, 11, induced air pipe, 12, first induced draft fan, 13, reinforcing rib, 14, first sealing device, 15, second sealing device, 16, cooler, 17, second induced draft fan , 18, burner, 19, refractory brick layer, 20 air mixer.
具体实施方式Detailed ways
下面将结合本发明中的实施例和附图,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在没有做出创造性劳动前提下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 in conjunction with the embodiments of the present invention and the accompanying drawings. Obviously, the described embodiments are only some of the embodiments of the present invention, not all of them. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the protection scope of the present invention.
如图所示,本实施例的高效节能环保炭化炉,包括下料机1、支架2、回转筒体3、转动装置4及出料装置5,回转筒体3安装在支架2上,支架2设置为两个,分别为前滚轮架和后滚轮架。前滚轮架的高度高于后滚轮架,使回转筒体3以左高右低的方式倾斜安装。转动装置4通过滚圈带动回转筒体3转动,滚圈与回转筒体3之间设置有滚圈垫板,使回转筒体3与滚圈的摩擦力增大,更有利于回转筒体3的有效转动。As shown in the figure, the high-efficiency, energy-saving and environmentally friendly carbonization furnace of this embodiment includes a blanking machine 1, a bracket 2, a rotary cylinder 3, a rotating device 4 and a discharge device 5, the rotary cylinder 3 is installed on the bracket 2, and the bracket 2 There are two sets, respectively a front roller frame and a rear roller frame. The height of the front roller frame is higher than the rear roller frame, so that the rotary cylinder 3 is installed obliquely in a way that the left side is high and the right side is low. The rotating device 4 drives the rotating cylinder 3 to rotate through the rolling ring, and a rolling ring backing plate is arranged between the rolling ring and the rotating cylinder 3 to increase the friction between the rotating cylinder 3 and the rolling ring, which is more conducive to the rotation of the rotating cylinder 3 effective rotation.
回转筒体3的右端设置有出料装置5,左端设置有下料机1,下料机1底端安装有下料器8。回转筒体3的内侧壁设置有耐火砖层19,耐火砖层19内侧均匀设置有若干炭化仓7,中空部分为烟道仓6。回转筒体3左下部的炭化仓7一端与下料器8连接,另一端与出料装置5连接。烟道仓6通过进气管9贯穿出料装置5的中空部分与混风器20连接,烟道仓6通过出气管10贯穿下料机1的中空部分将烟气排出;出料装置5的上部设置有引风管11,引风管11的外端与第一引风机12连接。The right end of the rotary cylinder 3 is provided with a discharge device 5 , the left end is provided with a feeder 1 , and a feeder 8 is installed at the bottom of the feeder 1 . A refractory brick layer 19 is arranged on the inner wall of the rotating cylinder 3 , and a number of carbonization bins 7 are evenly arranged on the inner side of the refractory brick layer 19 , and the hollow part is a flue bin 6 . One end of the carbonization bin 7 at the bottom left of the rotary cylinder 3 is connected to the feeder 8 , and the other end is connected to the discharge device 5 . The flue chamber 6 penetrates the hollow part of the discharge device 5 through the air inlet pipe 9 and is connected with the air mixer 20, and the flue chamber 6 penetrates the hollow part of the blanking machine 1 through the air outlet pipe 10 to discharge the smoke; the upper part of the discharge device 5 An air induction pipe 11 is provided, and the outer end of the air induction pipe 11 is connected with the first air induction fan 12 .
在烟道仓6内设置有若干加强筋13,由于炭化仓7受高温影响产生不同程度的膨胀变形。加强筋13可活动支撑固定炭化仓7。A number of reinforcing ribs 13 are arranged in the flue chamber 6, and the carbonization chamber 7 is affected by high temperature to produce different degrees of expansion and deformation. The reinforcing rib 13 can movably support and fix the carbonization bin 7 .
为保证烟道仓6与进气管9和出气管10之间的密闭性,烟道仓6和下料机1之间设置有第一密封装置14,与出料装置5之间设置有第二密封装置15。In order to ensure the airtightness between the flue bin 6 and the air inlet pipe 9 and the outlet pipe 10, a first sealing device 14 is arranged between the flue bin 6 and the unloading machine 1, and a second sealing device 14 is arranged between the flue bin 6 and the discharge device 5. Sealing device 15.
在出料装置5的底部设置有冷却器16,使高温炭化料冷却后排出。A cooler 16 is provided at the bottom of the discharge device 5 to cool the high-temperature carbonized material and then discharge it.
混风器20内近出料装置5端设置有第二引风机17,远离出料装置5端设置有燃烧器18。在此炭化炉初始工作时,由于进入的空气温度低,不能满足炭化所需的能量,因此需要打开燃烧器18,在第二引风机17的作用下,将低温空气燃烧成高温空气经进气管9进入烟道仓6供给炭化仓7能量。A second induced draft fan 17 is provided in the air mixer 20 near the end of the discharge device 5, and a burner 18 is provided at the end far away from the discharge device 5. When the carbonization furnace is initially working, due to the low temperature of the incoming air, it cannot meet the energy required for carbonization, so it is necessary to turn on the burner 18, and under the action of the second induced draft fan 17, the low-temperature air is burned into high-temperature air through the intake pipe 9 enters the flue chamber 6 to supply the carbonization chamber 7 with energy.
原料从下料机1进入炭化炉,经下料器8进入炭化炉的炭化仓7内,依靠重力作用向出料装置5方向下落。炭化炉的炭化仓7分段控制温度加热,从常温缓慢加热到550℃-600℃,原料在炭化炉的炭化仓7内经过热处理、低温干馏、热裂解后生产出的炭化料进入出料装置5,自由下落经冷却器16冷却后排出;原料在低温干馏过程中挥发出的干馏气通过第一引风机12控制与原料在炭化仓7内同向运动,干馏气进入出料装置5,经出料装置5上部的引风管11排出。排出后进入高温焚烧炉焚烧,焚烧后产生的高温气体一部分通过进气管9进入炭化炉的烟道仓6,与原料逆向运动间接加热原料,达到低温干馏效果。高温气体从进气管9进入,经烟道仓6逐步给炭化仓7内的原料加热,在出气管10温度降为低温气体排出炭化炉,然后在引风机的作用下经脱硫塔后排出。The raw material enters the carbonization furnace from the feeder 1, enters the carbonization bin 7 of the carbonization furnace through the feeder 8, and falls toward the discharge device 5 by gravity. The carbonization chamber 7 of the carbonization furnace controls the temperature heating in sections, and slowly heats from normal temperature to 550°C-600°C. The carbonized material produced by the raw material in the carbonization chamber 7 of the carbonization furnace undergoes heat treatment, low-temperature dry distillation, and thermal cracking enters the discharge device 5. Free fall and discharge after being cooled by the cooler 16; the retort gas volatilized by the raw material during the low-temperature carbonization process is controlled by the first induced draft fan 12 to move in the same direction as the raw material in the carbonization chamber 7, and the retort gas enters the discharge device 5 and passes through The draft pipe 11 on the top of the discharge device 5 is discharged. After being discharged, it enters the high-temperature incinerator for incineration. Part of the high-temperature gas generated after incineration enters the flue chamber 6 of the carbonization furnace through the inlet pipe 9, and moves inversely with the raw material to indirectly heat the raw material to achieve the effect of low-temperature dry distillation. The high-temperature gas enters from the inlet pipe 9, and gradually heats the raw materials in the carbonization chamber 7 through the flue chamber 6, and the temperature drops to low-temperature gas in the outlet pipe 10, and is discharged from the carbonization furnace, and then discharged through the desulfurization tower under the action of the induced draft fan.
其他高温气体可通过负压进入烘干炉用于烘干原料,或进入换热器,加热软化水供锅炉使用,或进入余热锅炉产生蒸汽供使用。Other high-temperature gas can enter the drying furnace through negative pressure to dry raw materials, or enter the heat exchanger to heat and soften water for boiler use, or enter the waste heat boiler to generate steam for use.
原料在本发明炭化炉的炭化仓内,通过焚烧后的高温气体进行间接加热,经过热处理、低温干馏、热裂解生产炭化料,不和空气接触,杜绝了固定碳的燃烧,有利于生产出得率高、品质好的炭化料。物料运动方向与高温气体流动方向相反且各自按自己的轨道运行,完全不接触。这样既可以有效地控制各段的温度,又可以杜绝高温气体内的杂质进入炭化料内,生产出的炭化料灰分低,强度大。炭化料的挥发分适中,堆积重高,品质好。本发明炭化炉利用原料炭化干馏时产生的干馏气经高温焚烧产生的热能为炭化过程提供热源,多余的热能烘干原料及通过余热锅炉产生蒸汽供其他使用。整个低温干馏过程无需补充燃料,降低能耗,减少排放,真正达到节能环保。The raw material is in the carbonization chamber of the carbonization furnace of the present invention, and is indirectly heated by the high-temperature gas after incineration, and is produced through heat treatment, low-temperature dry distillation, and thermal cracking to produce carbonized materials without contact with air, which prevents the combustion of fixed carbon, and is beneficial to the production of High-efficiency, high-quality carbonized material. The material movement direction is opposite to the flow direction of the high-temperature gas, and each runs on its own track without contact at all. In this way, the temperature of each section can be effectively controlled, and impurities in the high-temperature gas can be prevented from entering the carbonized material. The produced carbonized material has low ash content and high strength. The volatile content of the carbonized material is moderate, the bulk weight is high, and the quality is good. The carbonization furnace of the present invention utilizes the heat energy generated by high-temperature incineration of dry distillation gas generated during carbonization and carbonization of raw materials to provide heat source for the carbonization process, and the excess heat energy dries raw materials and generates steam for other uses through waste heat boilers. The entire low-temperature dry distillation process does not need to supplement fuel, which reduces energy consumption and emissions, and truly achieves energy saving and environmental protection.
上述实施方式旨在举例说明本发明可为本领域专业技术人员实现或使用,对上述实施方式进行修改对本领域的专业技术人员来说将是显而易见的,故本发明包括但不限于上述实施方式,任何符合本权利要求书或说明书描述,符合与本文所公开的原理和新颖性、创造性特点的方法、工艺、产品,均落入本发明的保护范围之内。The above embodiments are intended to illustrate that the present invention can be implemented or used by those skilled in the art. It will be obvious to those skilled in the art to modify the above embodiments, so the present invention includes but is not limited to the above embodiments. Any method, process, or product that conforms to the claims or the description of the specification, and conforms to the principles, novelty, and creative features disclosed herein falls within the protection scope of the present invention.
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