化工进展 ›› 2021, Vol. 40 ›› Issue (3): 1362-1370.DOI: 10.16085/j.issn.1000-6613.2020-0888
收稿日期:
2020-05-22
出版日期:
2021-03-05
发布日期:
2021-03-17
通讯作者:
范涛
作者简介:
范涛(1986—),男,博士研究生,研究方向为煤炭转化与清洁利用。E-mail:基金资助:
Received:
2020-05-22
Online:
2021-03-05
Published:
2021-03-17
Contact:
FAN Tao
摘要:
蒙东褐煤占我国褐煤储量的83%,是蒙东地区的主要能源。低温热解技术条件温和、产品用途广、经济效益高,是加工蒙东褐煤的主要途径之一。但由于褐煤块煤率低、含水量高、热碎严重等特性以及现行环保产业政策持续趋紧,使褐煤低温热解工业化项目存在原料利用率低、生产连续性差、环保不达标等问题。本文介绍了目前蒙东地区应用的热解技术包括低阶煤转化技术(LCC)、连续干馏热解定位提质技术(LCP)、带式炉低温干馏技术、GF-1型褐煤提质技术、SJ低温干馏方炉热解技术和气-固错流热解技术,分析了各项技术的运行情况、优势和不足。通过对比各项技术在原料要求、传热方式、熄焦方式、能量利用率和产品性质等方面的特点,明确了各项热解技术的炉型选择、原料煤粒度和热解产品利用等方向,提出了蒙东褐煤热解技术在工业化应用过程中需实现原料优化、能量优化、产品多元化和废弃物资源化的发展要求。
中图分类号:
范涛. 蒙东褐煤热解技术工业应用进展[J]. 化工进展, 2021, 40(3): 1362-1370.
FAN Tao. Industrial application progress of lignite pyrolysis technology in eastern area of Inner Mongolia, China[J]. Chemical Industry and Engineering Progress, 2021, 40(3): 1362-1370.
褐煤资源 | 工业分析(ar,质量分数)/% | 元素分析(daf,质量分数)/% | 热值Qnet,ar /MJ·kg-1 | ||||||
---|---|---|---|---|---|---|---|---|---|
M | A | V | C | H | N | S | O | ||
霍林河煤田 | 32.96 | 14.42 | 30.06 | 74.42 | 4.00 | 1.12 | 0.43 | 20.03 | 14.12 |
胜利煤田 | 33.24 | 9.30 | 22.28 | 66.90 | 4.16 | 1.03 | 2.10 | 25.81 | 15.62 |
白音华煤田 | 32.92 | 7.44 | 25.46 | 68.8 | 5.00 | 1.40 | 1.40 | 23.4 | 15.21 |
伊敏河煤田 | 30.24 | 10.36 | 26.15 | 68.95 | 4.97 | 0.97 | 0.32 | 25.09 | 14.75 |
元宝山煤田 | 30.55 | 10.10 | 22.24 | 79.15 | 4.86 | 1.37 | 0.57 | 14.05 | 12.55 |
乌拉盖褐煤 | 39.42 | 6.79 | 26.18 | 74.05 | 3.94 | 0.78 | 0.88 | 20.35 | 13.90 |
表1 蒙东地区典型褐煤的煤质分析
褐煤资源 | 工业分析(ar,质量分数)/% | 元素分析(daf,质量分数)/% | 热值Qnet,ar /MJ·kg-1 | ||||||
---|---|---|---|---|---|---|---|---|---|
M | A | V | C | H | N | S | O | ||
霍林河煤田 | 32.96 | 14.42 | 30.06 | 74.42 | 4.00 | 1.12 | 0.43 | 20.03 | 14.12 |
胜利煤田 | 33.24 | 9.30 | 22.28 | 66.90 | 4.16 | 1.03 | 2.10 | 25.81 | 15.62 |
白音华煤田 | 32.92 | 7.44 | 25.46 | 68.8 | 5.00 | 1.40 | 1.40 | 23.4 | 15.21 |
伊敏河煤田 | 30.24 | 10.36 | 26.15 | 68.95 | 4.97 | 0.97 | 0.32 | 25.09 | 14.75 |
元宝山煤田 | 30.55 | 10.10 | 22.24 | 79.15 | 4.86 | 1.37 | 0.57 | 14.05 | 12.55 |
乌拉盖褐煤 | 39.42 | 6.79 | 26.18 | 74.05 | 3.94 | 0.78 | 0.88 | 20.35 | 13.90 |
技术类别 | 规模/ | 原料粒度/mm | 传热方式 | 熄焦方式 | 是否补热 | 焦油品质 | 半焦用途 |
---|---|---|---|---|---|---|---|
LCC技术 | 30 | 6~50 | 内热式 | 湿法熄焦 | 需要 | 含尘量高 | 动力煤 |
LCP技术 | 100 | <80 | 外热式 | 干法熄焦 | 需要 | 不回收 | 动力煤、型煤 |
带式炉改性提质技术 | 100 | 3~25 | 内热式 | 干法熄焦 | 需要 | 不回收 | 动力煤 |
GF-1型褐煤提质技术 | 2×50 | 6~120 | 内热式 | 干法熄焦 | 不需要 | 含尘量高 | 动力煤、活性焦 |
SJ方炉热解技术 | 30 | 30~80 | 内热式 | 水熄焦 | 不需要 | 品质较好 | 动力煤 |
气-固错流热解技术 | 60 | <80 | 内热式 | 干法熄焦 | 不需要 | 品质较好 | 动力煤、洁净型煤 |
表2 蒙东褐煤热解技术对比
技术类别 | 规模/ | 原料粒度/mm | 传热方式 | 熄焦方式 | 是否补热 | 焦油品质 | 半焦用途 |
---|---|---|---|---|---|---|---|
LCC技术 | 30 | 6~50 | 内热式 | 湿法熄焦 | 需要 | 含尘量高 | 动力煤 |
LCP技术 | 100 | <80 | 外热式 | 干法熄焦 | 需要 | 不回收 | 动力煤、型煤 |
带式炉改性提质技术 | 100 | 3~25 | 内热式 | 干法熄焦 | 需要 | 不回收 | 动力煤 |
GF-1型褐煤提质技术 | 2×50 | 6~120 | 内热式 | 干法熄焦 | 不需要 | 含尘量高 | 动力煤、活性焦 |
SJ方炉热解技术 | 30 | 30~80 | 内热式 | 水熄焦 | 不需要 | 品质较好 | 动力煤 |
气-固错流热解技术 | 60 | <80 | 内热式 | 干法熄焦 | 不需要 | 品质较好 | 动力煤、洁净型煤 |
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