CN114806605A - Vertical carbonization furnace for gas coal coking - Google Patents
Vertical carbonization furnace for gas coal coking Download PDFInfo
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- CN114806605A CN114806605A CN202210556928.2A CN202210556928A CN114806605A CN 114806605 A CN114806605 A CN 114806605A CN 202210556928 A CN202210556928 A CN 202210556928A CN 114806605 A CN114806605 A CN 114806605A
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- 239000003245 coal Substances 0.000 title claims abstract description 123
- 238000003763 carbonization Methods 0.000 title claims abstract description 45
- 238000004939 coking Methods 0.000 title claims abstract description 23
- 238000012216 screening Methods 0.000 claims abstract description 25
- 238000003756 stirring Methods 0.000 claims description 16
- 238000010438 heat treatment Methods 0.000 abstract description 20
- 238000007873 sieving Methods 0.000 abstract 2
- 230000000712 assembly Effects 0.000 abstract 1
- 238000000429 assembly Methods 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 20
- 239000000463 material Substances 0.000 description 8
- 239000002699 waste material Substances 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 229910000997 High-speed steel Inorganic materials 0.000 description 2
- 235000013399 edible fruits Nutrition 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000003068 static effect Effects 0.000 description 2
- 239000004575 stone Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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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
- C10B1/02—Stationary retorts
- C10B1/04—Vertical retorts
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B1/00—Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
- B07B1/28—Moving screens not otherwise provided for, e.g. swinging, reciprocating, rocking, tilting or wobbling screens
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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
- C10B3/00—Coke ovens with vertical chambers
-
- 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
- C10B31/00—Charging devices
- C10B31/02—Charging devices for charging vertically
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
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- Organic Chemistry (AREA)
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Abstract
Description
技术领域technical field
本发明涉及炭化炉领域,具体的说是一种气煤炼焦用直立炭化炉。The invention relates to the field of carbonization furnaces, in particular to a vertical carbonization furnace for gas-coal coking.
背景技术Background technique
气煤是目前已探明炼焦煤储量中占有较大比例的煤种之一,气煤炼焦即以气煤为原料,在隔绝空气条件下,加热到950℃左右,经高温干馏生产焦炭,同时其他一些有用物质的一种煤转化工艺,直立炭化炉是目前气煤炼焦最常用的炭化炉之一。Gas coal is one of the coal types that has a large proportion in the proven coking coal reserves. Gas coal coking uses gas coal as raw material. Under the condition of isolated air, it is heated to about 950 ℃, and coke is produced by high temperature dry distillation. A coal conversion process for some other useful substances, the vertical carbonization furnace is one of the most commonly used carbonization furnaces for gas coal coking.
传统的炭化炉对气煤进行加热时,距离加热器越近,加热温度越高,气煤加热的越快,由于不同大小的气煤往往是混合在一块直接输送到炭化炉内进行加热,存在位于加热器较远的体积较大的气煤加热速度较慢,需要长时间加热的问题,因此传统的炭化炉无法对气煤进行高效的加热,对能源造成了一定的浪费。When the traditional carbonization furnace heats gas coal, the closer it is to the heater, the higher the heating temperature, and the faster the gas coal is heated. Since gas coals of different sizes are often mixed together and directly transported to the carbonization furnace for heating, there are The gas coal with a larger volume located farther away from the heater has a slow heating speed and requires a long time to heat. Therefore, the traditional carbonization furnace cannot efficiently heat the gas coal, resulting in a certain waste of energy.
鉴于此,为了克服上述技术问题,本发明设计了一种气煤炼焦用直立炭化炉,解决了上述技术问题。In view of this, in order to overcome the above technical problems, the present invention designs a vertical carbonization furnace for gas coal coking, which solves the above technical problems.
发明内容SUMMARY OF THE INVENTION
本发明所要解决的技术问题是:传统的炭化炉对气煤进行加热时,距离加热器越近的气煤加热越快,由于不同大小的气煤往往是混合在一块直接输送到炭化炉内进行加热,并未对其进行筛选,因此传统的炭化炉无法对气煤进行有效的加热,对能源造成了一定的浪费。The technical problem to be solved by the present invention is: when the traditional carbonization furnace heats the gas coal, the gas coal that is closer to the heater is heated faster, because the gas coal of different sizes is often mixed in one piece and directly transported to the carbonization furnace for heating. Therefore, the traditional carbonization furnace cannot effectively heat the gas coal, resulting in a certain waste of energy.
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:
本发明提供的一种气煤炼焦用直立炭化炉,包括底座、壳体和加热器,还包括:A vertical carbonization furnace for gas-coal coking provided by the present invention includes a base, a shell and a heater, and further includes:
筛动组件,所述筛动组件布置于壳体内,所述筛动组件对进入壳体内不同大小的气煤进行筛选;a screening assembly, the screening assembly is arranged in the casing, and the screening assembly screens gas coals of different sizes entering the casing;
动力组件,所述动力组件设置在壳体的一侧,且与筛动组件相连,所述动力组件用于在筛动组件工作时为其提供动力。The power assembly is arranged on one side of the casing and is connected with the screen moving assembly, and the power assembly is used for providing power to the screen moving assembly when it works.
优选的,所述筛动组件包括均匀布置于壳体内的一号移动板、二号移动板和三号移动板;Preferably, the sieve assembly includes a No. 1 moving plate, a No. 2 moving plate and a No. 3 moving plate that are evenly arranged in the housing;
一号筛盒,设置于一号移动板表面;No. 1 sieve box, set on the surface of No. 1 moving plate;
二号筛盒,设置于二号移动板表面;The No. 2 sieve box is arranged on the surface of the No. 2 moving plate;
三号筛盒,设置于三号移动板表面;No. 3 sieve box, set on the surface of No. 3 moving plate;
凹槽和一号通孔,开设于壳体内表面;The groove and the No. 1 through hole are opened on the inner surface of the shell;
弹簧,设置在凹槽内。The spring is arranged in the groove.
优选的,所述动力组件包括机壳,所述机壳与壳体固定连接,且位于壳体一侧;Preferably, the power assembly includes a casing, the casing is fixedly connected to the casing, and is located on one side of the casing;
二号通孔,开设于机壳内表面,且与一号通孔相连通;The No. 2 through hole is opened on the inner surface of the casing and communicated with the No. 1 through hole;
电机,与机壳固定连接,且位于机壳上表面;The motor is fixedly connected to the casing and is located on the upper surface of the casing;
转轴,与电机固定连接;The rotating shaft is fixedly connected with the motor;
凸轮,设置于转轴上。The cam is arranged on the rotating shaft.
优选的,所述一号筛盒、二号筛盒和三号筛盒的体积依次增大。Preferably, the volumes of the No. 1 sieve box, the No. 2 sieve box and the No. 3 sieve box are sequentially increased.
优选的,所述一号筛盒和二号筛盒上固定连接有圆杆,所述一号移动板和二号移动板上均开设有滑槽,所述圆杆的两端位于滑槽内。Preferably, a round bar is fixedly connected to the No. 1 screen box and the No. 2 screen box, a chute is provided on the No. 1 moving plate and the No. 2 moving plate, and both ends of the round bar are located in the chute .
优选的,所述圆杆位于一号筛盒和二号筛盒的中间位置。Preferably, the round bar is located in the middle of the No. 1 sieve box and the No. 2 sieve box.
优选的,所述圆杆上固定连接有平衡块。Preferably, a balance block is fixedly connected to the round rod.
优选的,所述一号筛盒、二号筛盒和三号筛盒的内表面固定连接有搅拌件。Preferably, stirring elements are fixedly connected to the inner surfaces of the No. 1 sieve box, the No. 2 sieve box and the No. 3 sieve box.
优选的,所述一号筛盒、二号筛盒和三号筛盒的底部开设有三号通孔。Preferably, the No. 1 sieve box, the No. 2 sieve box and the No. 3 sieve box are provided with a No. 3 through hole at the bottom.
优选的,所述一号移动板和二号移动板的结构为中空结构。Preferably, the structures of the No. 1 moving plate and the No. 2 moving plate are hollow structures.
优选的,所述筛动组件、动力组件、圆杆、平衡块和搅拌件的材料为耐高温材料。Preferably, the materials of the screening component, power component, round rod, balance block and stirring member are high temperature resistant materials.
本发明的有益效果如下:The beneficial effects of the present invention are as follows:
1.本发明通过在壳体一侧安装的动力组件驱动壳体内的筛动组件左右往复运动,从而对进入壳体内不同大小的气煤进行筛选,使较大的气煤靠近加热器,较小的气煤远离加热器,以使炭化炉对气煤加热更加高效,达到节约能源的效果。1. The present invention drives the left and right reciprocating motion of the screen assembly in the casing by the power assembly installed on one side of the casing, so as to screen the gas coals of different sizes entering the casing, so that the larger gas coal is close to the heater, and the smaller one is close to the heater. The gas coal is kept away from the heater, so that the carbonization furnace can heat the gas coal more efficiently and achieve the effect of saving energy.
2.本发明通过在一号筛盒和二号筛盒上固定连接有圆杆,使圆杆与一号移动板和二号移动板上的滑槽相互配合,使一号筛盒和二号筛盒在往复运动的同时发生一定角度的摇摆晃动,以使一号筛盒和二号筛盒内较大的气煤能够快速从一号筛盒和二号筛盒内掉出,从而达到对不同大小的气煤快速筛选的效果。2. In the present invention, a round bar is fixedly connected to the No. 1 sieve box and the No. 2 sieve box, so that the round bar and the chute on the No. 1 moving plate and the No. 2 moving plate cooperate with each other, so that the No. 1 sieve box and the No. The screen box shakes at a certain angle while reciprocating, so that the larger gas coal in the No. 1 screen box and the No. 2 screen box can quickly fall out of the No. 1 screen box and No. The effect of rapid screening of gas coals of different sizes.
附图说明Description of drawings
为了更清楚地说明本发明具体实施方式或现有技术中的技术方案,下面将对具体实施方式或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图是本发明的一些实施方式,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the specific embodiments of the present invention or the technical solutions in the prior art, the accompanying drawings required in the description of the specific embodiments or the prior art will be briefly introduced below. The drawings are some embodiments of the present invention. For those of ordinary skill in the art, other drawings can also be obtained based on these drawings without creative efforts.
图1是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是本发明的筛动组件和动力组件运动状态示意图;2 is a schematic diagram of the motion state of the screen assembly and the power assembly of the present invention;
图3是本发明的图1中A处的放大示意图;Fig. 3 is the enlarged schematic diagram of A place in Fig. 1 of the present invention;
图4是本发明的一号移动板、一号筛盒和圆杆的位置结构示意图。4 is a schematic diagram of the position and structure of the No. 1 moving plate, the No. 1 screen box and the round rod of the present invention.
图中:底座1、壳体2、凹槽21、一号通孔22、加热器3、筛动组件4、一号移动板41、滑槽411、二号移动板42、三号移动板43、一号筛盒44、三号通孔441、二号筛盒45、三号筛盒46、弹簧47、动力组件5、机壳51、二号通孔511、电机52、转轴53、凸轮54、圆杆6、平衡块7、搅拌件8。In the figure:
具体实施方式Detailed ways
为了使本发明实现的技术手段、创作特征、达成目的与功效易于明白了解,下面结合具体实施方式,进一步阐述本发明。In order to make it easy to understand the technical means, creation features, achieved goals and effects of the present invention, the present invention will be further described below with reference to the specific embodiments.
本发明实施例通过一种气煤炼焦用直立炭化炉,解决了现有技术中,炭化炉对气煤进行加热时,距离加热器越近,加热温度越高,气煤加热的越快,由于不同大小的气煤往往是混合在一块直接输送到炭化炉内进行加热,存在位于加热器较远的体积较大的气煤加热速度较慢,需要长时间加热的问题,因此传统的炭化炉无法对气煤进行高效的加热,对能源造成了一定的浪费的问题。The embodiment of the present invention solves the problem that in the prior art, when the carbonization furnace heats the gas coal, the closer the distance to the heater, the higher the heating temperature and the faster the gas coal heating. Gas coals of different sizes are often mixed in one piece and directly transported to the carbonization furnace for heating. There is a problem that the heating speed of larger gas coals located farther from the heater is slower and requires long-term heating. Therefore, traditional carbonization furnaces cannot be used. Efficient heating of gas coal causes a certain waste of energy.
本发明为了解决上述技术问题,总体构思如下:通过在壳体1一侧安装的动力组件5驱动壳体1内的筛动组件4左右往复运动,从而对进入壳体1内不同大小的气煤进行筛选,使较大的气煤靠近加热器3,较小的气煤远离加热器3,以使炭化炉对气煤加热更加高效,达到节约能源的效果。In order to solve the above technical problems, the general idea of the present invention is as follows: the
为了更好的理解上述技术方案,下面将结合说明书附图以及具体的实施方式对上述技术方案进行详细的说明。In order to better understand the above technical solutions, the above technical solutions will be described in detail below with reference to the accompanying drawings and specific embodiments.
本发明提供了一种气煤炼焦用直立炭化炉,包括底座1、壳体2和加热器3,还包括:The present invention provides a vertical carbonization furnace for gas-coal coking, comprising a
筛动组件4,所述筛动组件4均匀布置于壳体2内,所述筛动组件4对进入到壳体2内的不同大小的气煤进行筛选以实现对进入壳体2内部的气煤依据其体积大小进行堆放;The
动力组件5,所述动力组件5设置在壳体2的一侧且与筛动组件4相连,所述动力组件5给筛动组件4提供动力。A
传统的炭化炉是在底座1上方固定连接有供放置气煤的壳体2,在底座1内开设有空腔,在空腔内安装有加热器3,通过加热器3对底座1上的壳体2进行加热,因此在对气煤进行加热时,距离加热器3越近,加热温度越高,由于不同大小的气煤往往是混合在一块直接输送到炭化炉内进行加热,并未对其进行筛选,因此传统的炭化炉无法对气煤进行高效的加热,对能源造成了一定的浪费;In the traditional carbonization furnace, a
因此本发明在壳体2一侧固定连接有动力组件5,通过动力组件5驱动壳体2内的筛动组件4左右往复运动,当气煤从壳体2上方的进料口进入后落到筛动组件4上,由于筛动组件4左右往复运动,从而对进入壳体2内不同大小的气煤进行筛选,使较大的气煤靠近加热器3,较小的气煤远离加热器3,相对于传统的炭化炉直接对气煤进行加热,本发明对筛选后的气煤进行加热,从而使炭化炉对气煤加热更加高效,达到节约能源的效果。Therefore, in the present invention, a
作为本发明的一种具体实施方式,所述筛动组件4包括均匀布置于壳体2内的一号移动板41、二号移动板42和三号移动板43;As a specific embodiment of the present invention, the
一号筛盒44,设置于一号移动板41表面;The No. 1
二号筛盒45,设置于二号移动板42表面;The No. 2
三号筛盒46,设置于三号移动板43表面;The No. 3
凹槽21和一号通孔22,开设于壳体2内表面;The
弹簧47,设置在凹槽21内。The
作为本发明的一种具体实施方式,所述动力组件5包括机壳51,所述机壳51与壳体2固定连接,且位于壳体2一侧;As a specific embodiment of the present invention, the
二号通孔511,开设于机壳51内表面,且与一号通孔22相连通;The No. 2 through
电机52,与机壳51固定连接,且位于机壳51上表面;The
转轴53,与电机52固定连接;The rotating
凸轮54,设置于转轴53上。The
本发明通过在壳体2内表面开设有凹槽21和一号通孔22,机壳51内表面开设二号通孔511,且二号通孔511与一号通孔22相连通,壳体2内滑动连接有一号移动板41、二号移动板42和三号移动板43,一号移动板41、二号移动板42和三号移动板43的一端位于凹槽21内,另一端穿过一号通孔22和二号通孔511位于机壳51内,凹槽21内表面均固定连接有弹簧47,且弹簧47的另一端分别与对应的一号移动板41、二号移动板42和三号移动板43的一端固定连接,在一号移动板41、二号移动板42和三号移动板43上滑动连接有一号筛盒44、二号筛盒45和三号筛盒46,在机壳51的上表面固定连接有电机52,电机52的驱动轴上固定连接有转轴53,在转轴53上固定连接有凸轮54;In the present invention, a
当启动电机52时,电机52通过转轴53带动凸轮54转动,凸轮54分别带动与之相对应的一号移动板41、二号移动板42和三号移动板43向左运动,一号移动板41、二号移动板42和三号移动板43挤压凹槽21内的弹簧47,弹簧47由于自身的弹力推动一号移动板41、二号移动板42和三号移动板43向右运动,转轴53转动带动凸轮54转动,再次推动与之对应的一号移动板41、二号移动板42和三号移动板43向左运动,从而使一号移动板41、二号移动板42和三号移动板43做左右往复运动,由于一号筛盒44、二号筛盒45和三号筛盒46分别和一号移动板41、二号移动板42和三号移动板43滑动连接,因此一号移动板41、二号移动板42和三号移动板43带动一号筛盒44、二号筛盒45和三号筛盒46做往复运动,同时一号筛盒44、二号筛盒45和三号筛盒46在一号移动板41、二号移动板42和三号移动板43上的行程要小于一号移动板41、二号移动板42和三号移动板43左右移动的距离,以防止一号筛盒44、二号筛盒45和三号筛盒46在一号移动板41、二号移动板42和三号移动板43由于滑槽411的存在会相对静止;When the
当不同大小的气煤从壳体2上方的进料口进入后先落到一号筛盒44内,随着一号筛盒44左右做往复运动,一号筛盒44内不同大小的气煤由于受到巴西核果效应的影响,较小的气煤由于体积小处于一号筛盒44的下层,较大的气煤由于体积大则处于一号筛盒44的上层,随着气煤不断进入到壳体2内,处于一号筛盒44上层的较大的气煤掉落到二号筛盒45内,同理,随着气煤不断进入到壳体2内,处于二号筛盒45上层的较大的气煤掉落到三号筛盒46内,处于三号筛盒46上层的最大的气煤掉落到壳体2底部,使大多数最大体积的气煤位于距离加热器3最近的壳体2最底层,大多数中等体积的气煤位于壳体2距离加热器3较远的中间,大多数最小体积的气煤位于距离加热器3最远的壳体2的最上层,从而实现对不同大小的气煤筛选的效果,使炭化炉对气煤加热更加高效,达到节约能源的效果,由于气煤无法在层状结构的炭化炉内结焦,因此气煤要持续往壳体2内输送,直至与一号筛盒44的高度持平,以达到便于炼焦的效果。由于一号筛盒44、二号筛盒45和三号筛盒46的往复运动,也使得筛选的气煤分散的更加的均匀,从而使气煤达到受热均匀的效果。When the gas coal of different sizes enters from the feed port above the
作为本发明的一种具体实施方式,所述一号筛盒44、二号筛盒45和三号筛盒46的体积依次增大。As a specific embodiment of the present invention, the volumes of the No. 1
当一号筛盒44和二号筛盒45内较大的气煤向下掉落时,为了使掉落的气煤能够分别掉落到二号筛盒45和三号筛盒46内,本发明通过将一号筛盒44、二号筛盒45和三号筛盒46的体积由上到下依次增大,以保证一号筛盒44和二号筛盒45掉落的大多数的气煤能够分别落到二号筛盒45和三号筛盒46内,使二号筛盒45和三号筛盒46更好的对不同大小的气煤进行筛选。When the larger gas coal in the No. 1
作为本发明的一种具体实施方式,所述一号筛盒44和二号筛盒45上固定连接有圆杆6,所述一号移动板41和二号移动板42上均开设有滑槽411,所述圆杆6的两端位于滑槽411内。As a specific embodiment of the present invention, the No. 1
本发明通过在一号筛盒44和二号筛盒45上固定连接有圆杆6,在一号移动板41和二号移动板42上均开设有滑槽411,使圆杆6的两端位于滑槽411内,由于一号筛盒44和二号筛盒45底部固定连接有圆杆6,当一号筛盒44和二号筛盒45运动时,一号筛盒44和二号筛盒45会发生一定角度的摇摆晃动,以使一号筛盒44和二号筛盒45内较大的气煤能够快速从一号筛盒44和二号筛盒45内掉出,从而达到对不同大小的气煤快速筛选的效果。In the present invention,
作为本发明的一种具体实施方式,所述圆杆6位于一号筛盒44和二号筛盒45的中间位置。As a specific embodiment of the present invention, the
作为本发明的一种具体实施方式,所述圆杆6上固定连接有平衡块7。As a specific embodiment of the present invention, a
由于一号筛盒44和二号筛盒45在运动的同时需要一定角度的摇摆晃动,为了防止一号筛盒44和二号筛盒45发生侧翻的情况,本发明通过将圆杆6固定在一号筛盒44和二号筛盒45的中间位置,且在圆杆6上固定连接有平衡块7,以使一号筛盒44和二号筛盒45在多方向运动的情况保证其平衡的效果。Since the No. 1
作为本发明的一种具体实施方式,所述一号筛盒44、二号筛盒45和三号筛盒46的内表面固定连接有搅拌件8。As a specific embodiment of the present invention, a stirring
本发明通过在一号筛盒44、二号筛盒45和三号筛盒46的内表面固定连接有搅拌件8,在一号筛盒44、二号筛盒45和三号筛盒46在往复运动的同时,带动气煤碰撞搅拌件8,在气煤晃动的过程中,搅拌件8能够对晃动的气煤进行进一步的搅拌,使气煤受热更加均匀。In the present invention, the stirring
作为本发明的一种具体实施方式,所述一号筛盒44、二号筛盒45和三号筛盒46的底部开设有三号通孔441。As a specific embodiment of the present invention, the No. 1
由于气煤炼焦时会产生焦油,因此本发明通过在一号筛盒44、二号筛盒45和三号筛盒46的底部开设有三号通孔441,以便于一号筛盒44、二号筛盒45和三号筛盒46内的焦油及时流出。Since tar will be produced when gas coal is coking, the present invention has a third through
作为本发明的一种具体实施方式,所述一号移动板41和二号移动板42的结构为中空结构。As a specific embodiment of the present invention, the structures of the No. 1 moving
本发明通过将一号移动板41和二号移动板42的结构做成中空结构,当一号筛盒44和二号筛盒45内的气煤掉落时,能够分别从一号移动板41和二号移动板42的中空处穿过直接掉落到二号筛盒45和三号筛盒46内进行筛选,以达到快速筛选的效果。In the present invention, by making the structures of the No. 1 moving
作为本发明的一种具体实施方式,所述筛动组件4、动力组件5、圆杆6、平衡块7和搅拌件8的材料为耐高温材料。As a specific embodiment of the present invention, the materials of the
由于本发明的工作温度500℃-1000℃,,因此本发明中筛动组件4、动力组件5、圆杆6、平衡块7和搅拌件8的材料为耐高温材料,例如高速钢、3Cr2W8V、5CrNiMo、5CrMnMo等,以使其能够正常运动。Since the working temperature of the present invention is 500°C to 1000°C, the materials of the
工作原理:传统的炭化炉是在底座1上方固定连接有供放置气煤的壳体2,在底座1内开设有空腔,在空腔内安装有加热器3,通过加热器3对底座1上的壳体2进行加热,因此在对气煤进行加热时,距离加热器3越近,加热温度越高,由于不同大小的气煤往往是混合在一块直接输送到炭化炉内进行加热,并未对其进行筛选,因此传统的炭化炉无法对气煤进行高效的加热,对能源造成了一定的浪费;Working principle: The traditional carbonization furnace is fixedly connected with a
因此本发明在壳体2一侧固定连接有动力组件5,通过动力组件5驱动壳体2内的筛动组件4左右往复运动,当气煤从壳体2上方的进料口进入后落到筛动组件4上,由于筛动组件4左右往复运动,从而对进入壳体2内不同大小的气煤进行筛选,使较大的气煤靠近加热器3,较小的气煤远离加热器3,相对于传统的炭化炉直接对气煤进行加热,本发明对筛选后的气煤进行加热,从而使炭化炉对气煤加热更加高效,达到节约能源的效果。Therefore, in the present invention, a
本发明通过在壳体2内表面开设有凹槽21和一号通孔22,机壳51内表面开设二号通孔511,且二号通孔511与一号通孔22相连通,壳体2内滑动连接有一号移动板41、二号移动板42和三号移动板43,一号移动板41、二号移动板42和三号移动板43的一端位于凹槽21内,另一端穿过一号通孔22和二号通孔511位于机壳51内,凹槽21内表面均固定连接有弹簧47,且弹簧47的另一端分别与对应的一号移动板41、二号移动板42和三号移动板43的一端固定连接,在一号移动板41、二号移动板42和三号移动板43上滑动连接有一号筛盒44、二号筛盒45和三号筛盒46,在机壳51的上表面固定连接有电机52,电机52的驱动轴上固定连接有转轴53,在转轴53上固定连接有凸轮54;In the present invention, a
当启动电机52时,电机52通过转轴53带动凸轮54转动,凸轮54分别带动与之相对应的一号移动板41、二号移动板42和三号移动板43向左运动,一号移动板41、二号移动板42和三号移动板43挤压凹槽21内的弹簧47,弹簧47由于自身的弹力推动一号移动板41、二号移动板42和三号移动板43向右运动,转轴53转动带动凸轮54转动,再次推动与之对应的一号移动板41、二号移动板42和三号移动板43向左运动,从而使一号移动板41、二号移动板42和三号移动板43做左右往复运动,由于一号筛盒44、二号筛盒45和三号筛盒46分别和一号移动板41、二号移动板42和三号移动板43滑动连接,因此一号移动板41、二号移动板42和三号移动板43带动一号筛盒44、二号筛盒45和三号筛盒46做往复运动,同时一号筛盒44、二号筛盒45和三号筛盒46在一号移动板41、二号移动板42和三号移动板43上的行程要小于一号移动板41、二号移动板42和三号移动板43左右移动的距离,以防止一号筛盒44、二号筛盒45和三号筛盒46在一号移动板41、二号移动板42和三号移动板43由于滑槽411的存在会相对静止;When the
当不同大小的气煤从壳体2上方的进料口进入后先落到一号筛盒44内,随着一号筛盒44左右做往复运动,一号筛盒44内不同大小的气煤由于受到巴西核果效应的影响,较小的气煤由于体积小处于一号筛盒44的下层,较大的气煤由于体积大则处于一号筛盒44的上层,随着气煤不断进入到壳体2内,处于一号筛盒44上层的较大的气煤掉落到二号筛盒45内,同理,随着气煤不断进入到壳体2内,处于二号筛盒45上层的较大的气煤掉落到三号筛盒46内,处于三号筛盒46上层的最大的气煤掉落到壳体2底部,使大多数最大体积的气煤位于距离加热器3最近的壳体2最底层,大多数中等体积的气煤位于壳体2距离加热器3较远的中间,大多数最小体积的气煤位于距离加热器3最远的壳体2的最上层,从而实现对不同大小的气煤筛选的效果,使炭化炉对气煤加热更加高效,达到节约能源的效果,由于气煤无法在层状结构的炭化炉内结焦,因此气煤要持续往壳体2内输送,直至与一号筛盒44的高度持平,以达到便于炼焦的效果。由于一号筛盒44、二号筛盒45和三号筛盒46的往复运动,也使得筛选的气煤分散的更加的均匀,从而使气煤达到受热均匀的效果。When the gas coal of different sizes enters from the feed port above the
当一号筛盒44和二号筛盒45内较大的气煤向下掉落时,为了使掉落的气煤能够分别掉落到二号筛盒45和三号筛盒46内,本发明通过将一号筛盒44、二号筛盒45和三号筛盒46的体积由上到下依次增大,以保证一号筛盒44和二号筛盒45掉落的大多数的气煤能够分别落到二号筛盒45和三号筛盒46内,使二号筛盒45和三号筛盒46更好的对不同大小的气煤进行筛选。When the larger gas coal in the No. 1
本发明通过在一号筛盒44和二号筛盒45上固定连接有圆杆6,在一号移动板41和二号移动板42上均开设有滑槽411,使圆杆6的两端位于滑槽411内,由于一号筛盒44和二号筛盒45底部固定连接有圆杆6,当一号筛盒44和二号筛盒45运动时,一号筛盒44和二号筛盒45会发生一定角度的摇摆晃动,以使一号筛盒44和二号筛盒45内较大的气煤能够快速从一号筛盒44和二号筛盒45内掉出,从而达到对不同大小的气煤快速筛选的效果。In the present invention,
由于一号筛盒44和二号筛盒45在运动的同时需要一定角度的摇摆晃动,为了防止一号筛盒44和二号筛盒45发生侧翻的情况,本发明通过将圆杆6固定在一号筛盒44和二号筛盒45的中间位置,且在圆杆6上固定连接有平衡块7,以使一号筛盒44和二号筛盒45在多方向运动的情况保证其平衡的效果。Since the No. 1
本发明通过在一号筛盒44、二号筛盒45和三号筛盒46的内表面转动连接有搅拌件8,在一号筛盒44、二号筛盒45和三号筛盒46在往复运动的同时,带动气煤碰撞搅拌件8,在气煤晃动的过程中,搅拌件8能够对晃动的气煤进行进一步的搅拌,使气煤受热更加均匀。In the present invention, the stirring
由于气煤炼焦时会产生焦油,因此本发明通过在一号筛盒44、二号筛盒45和三号筛盒46的底部开设有三号通孔441,以便于一号筛盒44、二号筛盒45和三号筛盒46内的焦油及时流出。Since tar will be produced when gas coal is coking, the present invention has a third through
本发明通过将一号移动板41和二号移动板42的结构做成中空结构,当一号筛盒44和二号筛盒45内的气煤掉落时,能够分别从一号移动板41和二号移动板42的中空处穿过直接掉落到二号筛盒45和三号筛盒46内进行筛选,以达到快速筛选的效果。In the present invention, by making the structures of the No. 1 moving
由于本发明的工作温度为500℃-1000℃,因此本发明中筛动组件4、动力组件5、圆杆6、平衡块7和搅拌件8的材料为耐高温材料,例如高速钢、3Cr2W8V、5CrNiMo、5CrMnMo等,以使其能够正常运动。Since the working temperature of the present invention is 500°C-1000°C, the materials of the
以上显示和描述了本发明的基本原理、主要特征和优点。本行业的技术人员应该了解,本发明不受上述实施例的限制,上述实施例和说明书中描述的只是说明本发明的原理,在不脱离本发明精神和范围的前提下,本发明还会有各种变化和改进,这些变化和改进都落入要求保护的本发明范围内。本发明要求保护范围由所附的权利要求书及其等效物界定。The foregoing has shown and described the basic principles, main features and advantages of the present invention. Those skilled in the art should understand that the present invention is not limited by the above-mentioned embodiments. The above-mentioned embodiments and descriptions only illustrate the principle of the present invention. Without departing from the spirit and scope of the present invention, the present invention will also have Various changes and modifications fall within the scope of the claimed invention. The claimed scope of the present invention is defined by the appended claims and their equivalents.
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CN111635768B (en) * | 2020-07-05 | 2024-11-05 | 昆明理工大学 | A portable carbonization furnace for in-situ resource utilization of agricultural waste and graded preparation of biochar in the field |
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