CN112342067A - 含尘焦油成型利用的方法 - Google Patents

含尘焦油成型利用的方法 Download PDF

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CN112342067A
CN112342067A CN202011154062.XA CN202011154062A CN112342067A CN 112342067 A CN112342067 A CN 112342067A CN 202011154062 A CN202011154062 A CN 202011154062A CN 112342067 A CN112342067 A CN 112342067A
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陈元应
王伟东
陈爱平
梅长松
李春启
刘永健
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Datang International Chemical Technology Research Institute Co Ltd
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    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/02Fixed-bed gasification of lump fuel
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    • C10L5/00Solid fuels
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    • C10L5/48Solid fuels essentially based on materials of non-mineral origin on industrial residues and waste materials
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    • C10L9/10Treating solid fuels to improve their combustion by using additives
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/09Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0903Feed preparation
    • C10J2300/0906Physical processes, e.g. shredding, comminuting, chopping, sorting
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    • C10J2300/00Details of gasification processes
    • C10J2300/09Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
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Abstract

本发明提供一种含尘焦油成型利用的方法,其包括以下步骤:(1)将含尘焦油、粉煤、固体碱、添加剂混合,得到混合物料;(2)将所述混合物料挤压成块状物,然后将所述块状物自然阴干。本发明的方法能够使得含尘焦油成型,成型后的块状物不仅能够市售带来经济效益,还扩大了含尘焦油的利用方式,即,不仅作为进炉原料适用于普通锅炉,还能够适用于碎煤加压气化炉。本发明的方法不仅利用了含尘焦油,还充分利用了近乎废弃的粉状褐煤,具有非常大的经济效益。

Description

含尘焦油成型利用的方法
技术领域
本发明属于化工领域。具体地,本发明涉及一种含尘焦油成型利用的方法。
背景技术
碎煤加压气化技术的主产物为一氧化碳、氢气和甲烷,同时副产焦油。含尘焦油为碎煤加压气化煤气水分离的一种副产品。
目前,含尘焦油不能市售,对含尘焦油的利用方式是经干燥后在工厂直接用于锅炉掺烧。一方面,含尘焦油目前也仅限于普通的锅炉掺烧,不能满足作为碎煤加压气化炉进料的要求。另一方面,如此直接烧掉含尘焦油并没有带来附加值且经济效益差。此外,在未来含尘焦油可能会被定义为微废。
目前急需一种能够充分且具有经济效益的再利用含尘焦油的方法。
发明内容
本发明的目的是提供一种含尘焦油成型利用的方法,该方法优化了含尘焦油的利用,能够提高经济效益。
本发明的上述目的是通过如下技术方案实现的。
本发明提供一种含尘焦油成型利用的方法,其包括以下步骤:
(1)将含尘焦油、粉煤、固体碱、添加剂混合,得到混合物料;
(2)将所述混合物料挤压成块状物,然后将所述块状物自然阴干。
优选地,在本发明所述的方法中,所述含尘焦油为褐煤碎煤加压气化煤气水分离的副产物。
优选地,在本发明所述的方法中,所述含尘焦油中包含焦油、水和尘,且各组分的质量比为焦油:水:尘=45-50:5-10:40-50。
优选地,在本发明所述的方法中,所述步骤(1)中的粉煤是直径小于2mm的粉状褐煤。
本发明人发现粉煤的加入有利于含尘焦油的挤压成型,同时还利用了部分粉煤使得资源充分利用。
优选地,在本发明所述的方法中,所述步骤(1)中的固体碱是氢氧化钠、氢氧化钾、生石灰、固体水玻璃中的一种或几种。
本发明人发现碱性物质可以改善含尘焦油的成渣性能,有利于碎煤加压气化的排渣。
优选地,在本发明所述的方法中,所述步骤(1)中的添加剂是淀粉、膨润土、腐殖酸中的一种或几种。
本发明人发现添加剂起到粘结剂的作用,提高了焦油渣成型后产品的强度。
优选地,在本发明所述的方法中,所述步骤(1)中的固体碱与含尘焦油的质量比为0.05-0.3:1,优选为0.08-0.20:1。
优选地,在本发明所述的方法中,所述步骤(1)中的粉状褐煤与含尘焦油的质量比为0.5-4:1,优选为1-2:1。
优选地,在本发明所述的方法中,所述步骤(1)中的添加剂与含尘焦油的质量比为0.02-0.3:1,优选为0.05-0.15:1。
优选地,在本发明所述的方法中,所述步骤(2)中的挤压成块状物是在压力为15-35MPa的条件下进行的。
优选地,在本发明所述的方法中,所述步骤(2)中的块状物的尺寸为40-50mm。
本发明具有如下有益效果:
本发明的发明人经过研究发现,通过本发明的方法成型后的含尘焦油的强度满足碎煤加压气化炉对进炉原料强度的要求(大于400N)。
本发明的方法能够使得含尘焦油成型,成型后的块状物不仅能够市售带来经济效益,还扩大了含尘焦油的利用方式,即,不仅作为进炉原料适用于普通锅炉,还能够适用于碎煤加压气化炉。在碎煤加压气化炉中,块状物中的焦油进一步气化成一氧化碳、氢气和甲烷,提高了经济效益。
众所周知,粉状褐煤容易被大风刮走,不易储存,容易造成环境的严重污染。因此,如何实现粉状褐煤资源化利用成为褐煤行业的难点。本发明的方法不仅利用了含尘焦油,还充分利用了近乎废弃的粉状褐煤,具有非常大的经济效益。
具体实施方式
下面结合具体实施方式对本发明进行进一步的详细描述,给出的实施例仅为了阐明本发明,而不是为了限制本发明的范围。
实施例1
(1)将200g含尘焦油、400g粉状褐煤、22g氢氧化钠、10g淀粉混合均匀,得到混合物料;
(2)将混合物料在20MPa作用力下挤压成45mm的块状物,将块状物自然阴干。
采用强度检测仪检测阴干后块状物的强度为493N。
实施例2
(1)将200g含尘焦油、600g粉状褐煤、30g氢氧化钾、16g淀粉和8g腐殖酸混合均匀,得到混合物料;
(2)将混合物料在25MPa作用力下挤压成45mm的块状物,将块状物自然阴干。
采用强度检测仪检测阴干后块状物的强度为572N。
实施例3
(1)将200g含尘焦油、200g粉状褐煤、16g固体水玻璃、10g淀粉和10g膨润土混合均匀,得到混合物料;
(2)将混合物料在30MPa作用力下挤压成45mm的块状物,将块状物自然阴干。
采用强度检测仪检测阴干后块状物的强度为485N。
实施例4
(1)将200g含尘焦油、300g粉状褐煤、16g固体水玻璃、30g膨润土和8g腐殖酸混合均匀,得到混合物料;
(2)将混合物料在30MPa作用力下挤压成45mm的块状物,将块状物自然阴干。
采用强度检测仪检测阴干后块状物的强度为437N。

Claims (10)

1.一种含尘焦油成型利用的方法,其包括以下步骤:
(1)将含尘焦油、粉煤、固体碱、添加剂混合,得到混合物料;
(2)将所述混合物料挤压成块状物,然后将所述块状物自然阴干。
2.根据权利要求1所述的方法,其中,所述含尘焦油为褐煤碎煤加压气化煤气水分离的副产物。
3.根据权利要求1所述的方法,其中,所述含尘焦油中包含焦油、水和尘,且各组分的质量比为焦油:水:尘=45-50:5-10:40-50。
4.根据权利要求1所述的方法,其中,所述步骤(1)中的粉煤是直径小于2mm的粉状褐煤。
5.根据权利要求1所述的方法,其中,所述步骤(1)中的固体碱是氢氧化钠、氢氧化钾、生石灰、固体水玻璃中的一种或几种。
6.根据权利要求1所述的方法,其中,所述步骤(1)中的添加剂是淀粉、膨润土、腐殖酸中的一种或几种。
7.根据权利要求1所述的方法,其中,所述步骤(1)中的固体碱与含尘焦油的质量比为0.05-0.3:1,优选为0.08-0.20:1。
8.根据权利要求1所述的方法,其中,所述步骤(1)中的粉状褐煤与含尘焦油的质量比为0.5-4:1,优选为1-2:1。
9.根据权利要求1所述的方法,其中,所述步骤(1)中的添加剂与含尘焦油的质量比为0.02-0.3:1,优选为0.05-0.15:1。
10.根据权利要求1所述的方法,其中,所述步骤(2)中的挤压成块状物是在压力为15-35MPa的条件下进行的;
优选地,所述步骤(2)中的块状物的尺寸为40-50mm。
CN202011154062.XA 2020-10-26 2020-10-26 含尘焦油成型利用的方法 Pending CN112342067A (zh)

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20110197501A1 (en) * 2010-02-12 2011-08-18 Darrell Neal Taulbee Method for producing fuel briquettes from high moisture fine coal or blends of high moisture fine coal and biomass
CN105316066A (zh) * 2015-11-17 2016-02-10 中国科学院过程工程研究所 一种褐煤粘结剂成型制备加压气化型煤的方法
CN105950244A (zh) * 2016-07-21 2016-09-21 北京神雾环境能源科技集团股份有限公司 一种褐煤粉和生石灰粉成型用复合粘结剂
CN110564473A (zh) * 2019-08-22 2019-12-13 山西潞安煤基合成油有限公司 一种鲁奇炉用气化型焦的制备方法

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20110197501A1 (en) * 2010-02-12 2011-08-18 Darrell Neal Taulbee Method for producing fuel briquettes from high moisture fine coal or blends of high moisture fine coal and biomass
CN105316066A (zh) * 2015-11-17 2016-02-10 中国科学院过程工程研究所 一种褐煤粘结剂成型制备加压气化型煤的方法
CN105950244A (zh) * 2016-07-21 2016-09-21 北京神雾环境能源科技集团股份有限公司 一种褐煤粉和生石灰粉成型用复合粘结剂
CN110564473A (zh) * 2019-08-22 2019-12-13 山西潞安煤基合成油有限公司 一种鲁奇炉用气化型焦的制备方法

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Application publication date: 20210209