CN107255287B - 一种高含水率含油污泥的高效综合利用方法 - Google Patents
一种高含水率含油污泥的高效综合利用方法 Download PDFInfo
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- CN107255287B CN107255287B CN201710567452.1A CN201710567452A CN107255287B CN 107255287 B CN107255287 B CN 107255287B CN 201710567452 A CN201710567452 A CN 201710567452A CN 107255287 B CN107255287 B CN 107255287B
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- Prior art keywords
- oil
- flue gas
- oily sludge
- incineration
- mixture
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- 239000010802 sludge Substances 0.000 title claims abstract description 48
- 238000004064 recycling Methods 0.000 claims abstract description 8
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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[O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 74
- 239000003921 oils Substances 0.000 claims description 52
- 239000003546 flue gases Substances 0.000 claims description 50
- 239000000203 mixtures Substances 0.000 claims description 50
- 235000019198 oils Nutrition 0.000 claims description 49
- 239000003570 air Substances 0.000 claims description 35
- 239000000463 materials Substances 0.000 claims description 33
- 239000011901 water Substances 0.000 claims description 33
- 239000000779 smoke Substances 0.000 claims description 32
- 238000005303 weighing Methods 0.000 claims description 21
- 239000002028 Biomass Substances 0.000 claims description 20
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 20
- 229910052799 carbon Inorganic materials 0.000 claims description 20
- 239000007789 gases Substances 0.000 claims description 18
- 238000009825 accumulation Methods 0.000 claims description 17
- 125000004122 cyclic group Chemical group 0.000 claims description 16
- 238000002156 mixing Methods 0.000 claims description 16
- 239000011257 shell materials Substances 0.000 claims description 12
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/001—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals for sludges or waste products from water treatment installations
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
Abstract
Description
一种高含水率含油污泥的高效综合利用方法
技术领域
[0001]本发明属于固废无害化资源综合利用处理技术领域,具体涉及一种高含水率含油 污泥的高效综合利用方法。
背景技术
[0002]含油污泥,简称油泥,是石油开采、运输、炼制和含油污水处理过程中产生的固体 废物,其中,炼油厂污水处理场产生的油泥主要来源于隔油池底泥、浮选池浮渣、原油罐底 泥等,俗称“三泥”,这些油泥组成各异,通常含油率在i〇 %〜50 %之间,含水率在40 %〜 90%之间,含水率高,又极难脱水,导致“三泥”处理难度很大。
[0003]目前,我国的石化企业每年都有大量的含油污泥产生,由于缺乏适当的处理技术, 对“三泥”的处理一般为浓缩-沉降后转移到农村,不仅造成了二次污染,而且使得含油污泥 中的石油资源无法得到有效利用,造成了一定的经济损失。目前处理含油污泥的方法主要 有溶剂萃取法、焚烧法、生物处理法和焦化法等,其中,溶剂萃取法处理时间长、处理成本 高,技术不够成熟,且仅适用于含油量较高的含油污泥,性价比较低;生物处理法一般周期 较长,且不能回收原油,造成石油资源的浪费;焦化法涉及焦化装置的改造比较复杂,成本 高,且处理量少;目前的焚烧法无法直接处理高含水率的含油污泥,都需要脱水等预处理步 骤,增加了处理工序和成本,且由于“三泥”含油量低,焚烧时必须另外添加燃料油才能完成 焚烧过程,大大增加了炼油厂的能耗,如国内炼油厂每焚烧经脱水后含水率仍为75-85%的 “三泥”20-24吨,须添加1吨柴油做能源,过高的能耗使得炼油厂无法长期维持运行,目前国 内许多厂家的焚烧炉均处于闲置状态,此外,焚烧还存在热量回收率低,空气二次污染严重 等缺陷。
[0004]因此,研宄一种高效、绿色、综合利用处理高含水率含油污泥的方法,具有重要的 环保意义和经济效益。
发明内容
[0005]本发明的目的是提供一种高含水率含油污泥的高效综合利用方法,所述方法无需 脱水预处理,能够直接处理含水率高达40%-9〇%的含油污泥,且能够回收含油污泥中的原 油,提高了油泥处理的经济效益;此外,所述方法能够循环利用热能,大大降低了处理成本, 且不产生二次污染,能够实现含油污泥的高效、综合利用、清洁化处理。
[0006]为实现上述发明目的,本发明提供以下技术方案:
[0007] —种高含水率含油污泥的高效综合利用方法,包括以下步骤:
[0008]步骤1:将含水率为40 %_9〇 %的含油污泥与农作物粉碎物料、生石灰、生物质炭、 调质剂按质量比6〇_8〇: 5_10:3_5:0-10:2-10的比例混合制得混合物,所述的农作物粉碎物 料选自粒径为2-8mm的糠壳、秸秆和玉米芯等,所述的生物质炭粒径为,发热量为 4500-6500大卡,所述的调质剂为表面活性剂; ’ ^
[0009]步骤2:将步骤1所得的混合物送入负压循环蓄热回收系统的焚烧装置中,所述混 合物的厚度为350_7〇0麵,混合的行进速度〇-〇 • 2m/s,所述负压循环蓄热回收系统包括混合 装置(1)、焚烧装置⑵,抽风装置(3)、烟气循环装置⑷、油水收集装置(5)、传送装置⑹和 烟气净化装置(7),其特征在于:
[0010]所述混合装置(1)包括多个料仓(11)、计量称(12)、混合搅拌装置(13),所述料仓 (11)的出料口对准计量称(12)的称量盘,所述计量称(12)的称量盘与混合搅拌装置(13)的 进料口对应,料仓(11)内的农作物粉碎物料、生石灰、生物质炭和调质剂经计量称(12)称量 后,送入混合搅拌装置(1¾内与高含水率含油污泥混合搅拌得到步骤丨所述的混合物,混合 搅拌装置(13)的出料口连接传送装置(6),经传送装置(6)送入焚烧装置(2)中;
[0011]所述焚烧装置(2)由前至后依次包括布料段(20)、干燥段(21)、点火段(22)、焚烧 段(23)和冷却段(M),所述布料段(2〇)设有物料打散器(25),所述干燥段(21)的长度为1 -6m,点火段(22)的长度为l-3m,点火温度为85〇°C-105(TC,既能够避免混合物无法点燃的缺 陷,又能够避免温度过高引起的能耗高、混合物表层熔融影响透气性的缺陷,焚烧段(23)的 长度为4-2〇m,焚烧段温度为ll〇(TC,能够保证有害物质能得到充分的焚烧,所述干燥段 (21)和点火段(22)的上方设有从前至后由低到高的预热罩(26),与点火段(22)位置对应的 预热罩上设有废气进口(2乃和燃料喷嘴(%),形成二燃室,既对物料进行干燥预热,又将废 气进行深度处理,所述千燥段(21)、点火段(22)、焚烧段(23)和冷却段(24)的下方与抽风装 置⑶密封连接,所述焚烧段(2¾的上方与烟气循环系统⑷密封连接,步骤1所得混合物的 上部在点火段(22)点火后,在抽风装置(3)产生的负压作用下,火从混合物上部开始向下燃 烧,上部燃烧产生的高温蒸汽一方面对下部物料进行烘干和预热,另一方面将下部物料中 的水和油分带走,带出的油水混合物在重力作用下从底部流出进入油水收集装置(5);
[0012]所述抽风装置⑶包括多个抽风罩(31)、每个抽风罩(31)连接一套由抽风管(32) 和抽风机(33)组成的抽风管路,所述抽风管(32)和抽风机(33)之间设有油水收集装置(5), 与所述干燥段(21)下方连通的抽风管路的尾端与烟气净化装置(7)连通,与所述点火段 (2¾和焚烧段(23)下方连通的抽风管路的尾端与烟气循环装置(4)连通,与焚烧段(23)下 方连通的最后一级抽风管路的出口与预热罩(26)的废气进口(27)连通,与冷却段(24)下方 连通的抽风管路与机尾除尘装置连通;
[0013]所述的烟气循环装置(4)包括多个烟气罩(41),每个烟气罩(41)上均设有废气入 口(42)和新风配入口(43),所述烟气罩(41)的废气入口(42)与上一级抽风管路的尾端连 通,混合物料中的有害物质在高温焚烧中分解形成的烟气,经抽风罩(31)进入抽风管(32), 在油水收集装置(5)中进行烟气油水分离收集后,剩余烟气通过抽风机(33)送至下一级烟 气罩(41),完成对后段混合物料的干燥和预热,带出的油水混合物在重力作用下从底部流 出进入油水收集装置(5),与焚烧段(23)下方连通的最后一级抽风管路中的烟气通过废气 进口(27)进入预热罩(26)后,在二燃室进行二次燃烧,深度处理后进入烟气净化装置(7); [0014]所述油水收集装置(5)包括上部呈圆柱状,下部呈倒圆锥状的旋风式除油器(51), 所述旋风式除油器(51)的内部设有螺旋刮油板(52)、外壁设有与抽风管(32)的尾端连通的 烟气进口(53)、顶部设有与烟气罩(41)的废气入口(42)连通的烟气出口(54),底部与油水 收集器(55)连通,烟气和含油液滴经抽风管进入油水收集装置(5)后,含有液滴经螺旋刮油 板(52)与烟气分离,进入油水收集器(55),剩余烟气经烟气出口(54)进入下一级烟气罩 (41),实现石油的回收利用;
[0015] 所述烟气净化装置⑺的出气管经过抽风机连接至烟囱,将净化达标的废气排出。
[0016] 根据本发明所述的方法,步骤1中所述的农作物粉碎物料为粒径为2-8mra的糠壳, 且污泥、糠壳、生石灰、生物质炭和调质剂的质量比为60-75:6-10:3-5:2-8:5-10。
[0017] 本发明人发现,含油污泥、农作物粉碎物料、生石灰、生物质炭、调质剂五者的比例 对混合物的焚烧效果影响较大,当上述五者按质量比60-80:5-10:3-5:0-10:2-10的比例, 尤其是按质量比60-75:6-10:3-5:2-8:5-10的比例混合时,得到的混合物透气性好、热值水 平适当、焚烧速度适宜,燃烧充分,同时又能为含油液滴提供下流的通道。
[0018] 此外,农作物粉碎物料和生物质炭粒的粒径也对混合物的性质影响很大,当农作 物粉碎物料粒径或生物质炭粒粒径超过8mm时,制得的混合物透气性过好,焚烧速度过快, 燃烧不充分;当农作物粉碎物料粒径小于2mm或生物质炭粒粒径小于1mm时,制得的混合物 透气性差,风机负荷过大,焚烧不充分,且无法提供足够的油滴下流通道;本发明人通过大 量的试验发现,当农作物粉碎物料粒径为2-8mm或生物质炭粒粒径为l-8mm时,既能保证制 得的混合物的透气性,燃烧充分,又能为含油液滴提供足够的下流通道。
[0019] 根据本发明所述的方法,步骤2中所述的混合物厚度为500-700mm。
[0020] 本发明人还发现,混合物送入负压循环蓄热回收系统的焚烧装置时,厚度和行进 速度对焚烧效果也有很大影响,当厚度超过700_或行进速度超过〇. 2m/s时,混合物的透气 性不够,无法焚烧充分,影响焚烧效果;若厚度低于350mm时,混合物的蓄热效果差,焚烧温 度较低,无法充分分离出含油污泥中的石油,石油回收率低;只有控制混合物的厚度为350-700mm,且行进速度为0-0.2m/s时,既能保证混合物焚烧充分,又能有效回收混合物中的石 油,提高了固废处理的经济效益和处理效率,同时能够确保系统的稳定运行。
[0021] 根据本发明所述的方法,步骤2中所述的烟气装置(4)的新风配入口上设有进风管 调节阀,通过控制其开度控制新风的配入量。
[0022] 本发明的方法,利用负压循环蓄热焚烧装置的特点,添加一定的辅助物料,来实现 对含油污泥的处置,其特点是能够在对含油污泥中的有害物质进行焚烧处理的同时,利用 焚烧装置边焚烧边预热的特点,将污泥中的油类提取出来,实现对油类物质的回收利用,具 体优势如下:
[0023] 1、采用负压循环蓄热回收技术,有效利用上层物料焚烧产生的高温蒸汽对下部物 料进行烘干和预热,由于下部物料为湿物料,在上部产生的热蒸汽作用下,将混合料中的水 和油分带走,油水混合蒸汽遇到冷物料凝结成油水液滴,烟气的高温同时也可以降低粘度、 增加重油的流动性,液滴从底部流出,进行统一收集,大幅降低能耗和处理成本;
[0024] 2、能对高含水率含油污泥直接进行处理,解决了目前高含水率含油污泥的处置难 题;
[0025] 3、焚烧产生的烟气一方面通过抽风装置和烟气装置循环利用热能,一方面在抽风 装置和烟气装置的密封管路中运行,最终在二燃室深度处理后进入烟气净化装置,不产生 二次污染,能实现清洁化生产;
[0026] 4、采用了烟气多级循环二次燃烧技术,气体中的有害成分得到有效处理,同时燃 烧过程中废气的含氧量得到有效利用,因此大幅减少新进风量,进而大量减少烟气排放总 量,与一般焚烧方式烟气排放总量相比可减少6〇%以上;
[0027] 5、排放的水、气、渣均达到国家标准;
[0028] 6、污泥减量化、无害化、资源化程度高,效果明显;
[0029] 7、含油污泥的原油可进行回收;
[0030] 8、处理后的残渣达标后,可进行油井回填。
附图说明
[0031] 图1是本发明负压循环蓄热回收系统的结构示意图;
[0032] 图2是本发明负压循环蓄热回收系统混合装置的结构示意图;
[0033]图3是本发明负压循环蓄热回收系统焚烧装置、抽风装置、烟气循环装置、油水收 集装置和烟气净化装置的的结构示意图;
[0034]图4是本发明负压循环蓄热回收系统旋风式除油器的结构示意图;
[0035]图5是本发明的混合物焚烧原理示意图;
[0036]图6是本发明的方法流程图;
[0037]图中,
[0038] 1 —混合装置,11 —料仓,12 —计量称,13 —混合搅拌罐;
[0039] 2—焚烧装置,20—布料段,21—干燥段,22—点火段,23 —焚烧段,24 —冷却段, 25—物料打散器,26—预热罩,27—废气进口,28 —燃料喷嘴;
[0040] 3-抽风装置,31-抽风罩,32 —抽风管,33 —抽风机;
[0041] 4—烟气循环装置,41 —烟气罩,42—废气入口,43—新风配入口;
[0042] 5—油水收集装置,51—旋风式除油器,52 —螺旋刮油板,53—烟气进口,54—烟气 出口,55 —油水收集器;
[0043] 6—传送装置;
[0044] 7—烟气净化装置。
具体实施方式
[0045]实施例1负压循环蓄热回收系统
[0046]如图1-6所示,本发明的负压循环蓄热回收系统包括混合装置丨、焚烧装置2,抽风 装置3、烟气循环装置4、油水收集装置5、传送装置6和烟气净化装置7,所述混合装置1包括 多个料仓11、计量称12、混合搅拌装置13,所述料仓11的出料口对准计量称i 2的称量盘,所 述计量称12的称量盘与混合搅拌装置13的进料口对应,料仓11内的农作物粉碎物料、生石 灰、生物质炭和调质剂经计量称12称量后,送入混合搅拌装置13内与高含水率含油污泥混 合搅拌得到混合物,混合搅拌装置13的出料口连接传送装置6,经传送装置6送入焚烧装置2 中;
[0047]所述焚烧装置2由前至后依次包括布料段20、干燥段21、点火段22、焚烧段23和冷 却段24,所述布料段20设有物料打散器邪,所述干燥段21的长度为^伽,点火段22的长度 为l-em,点火温度为85(TC-l〇5(TC,既能够避免混合物无法点燃的缺陷,又能够避免温度过 高引起的能耗尚、混合物表层恪融影响透气性的缺陷,焚烧段23的长度为4-50m,焚烧段温 度为1100°C,能^保证有害物质能得到充分的焚烧,所述干燥段以和点火段22的上方设有 从前至后由低到高的预热罩26,与点火段22位置对应的预热罩上设有废气进口 27和燃料喷 嘴28,形成二燃室,既对物料进行干燥预热,又将废气进行深度处理,所述干燥段21、g火段 22、焚烧段23和冷却段奴的下方与抽风装置3密封连接,所述焚烧段23的上方与烟气循环系 统4密封连接,步骤1所得混合物的上部在点火段22点火后,在抽风装置3产生的负压作用 下,火从混合物上部开始向下燃烧,上部燃烧产生的高温蒸汽一方面对下部物料进行烘干 和预热,另一方面将下部物料中的水和油分带走,带出的油水混合物在重力作用下从底部 流出进入油水收集装置5;
[0048]所述抽风装置3包括多个抽风罩31、每个抽风罩31连接一套由抽风管32和抽风机 33组成的抽风管路,所述抽风管犯和抽风机33之间设有油水收集装置5,与所述干燥段21下 方连通的抽风管路的尾端与烟气净化装置7连通,与所述点火段22和焚烧段23下方连通的 抽风管路的尾端与烟气循环装置4连通,与焚烧段23下方连通的最后一级抽风管路的出口 与预热罩26的废气进口 27连通,与冷却段24下方连通的抽风管路与机尾除尘装置连通; [0049]所述的烟气循环装置4包括多个烟气罩41,每个烟气罩41上均设有废气入口 42和 新风配入口 43,所述烟气罩41的废气入口 42与上一级抽风管路的尾端连通,混合物料中的 有害物质在高温焚烧中分解形成的烟气,经抽风罩31进入抽风管32,在油水收集装置5中进 行烟气油水分离收集后,剩余烟气通过抽风机33送至下一级烟气罩41,完成对后段混合物 料的干燥和预热,实现了热能的传递,循环利用了热能,提高了经济效率,与焚烧段23下方 连通的最后一级抽风管路中的烟气通过废气进口 27进入预热罩26后,在二燃室进行二次燃 烧,深度处理后进入烟气净化装置7;
[0050]所述油水收集装置5包括上部呈圆柱状,下部呈倒圆锥状的旋风式除油器51,所述 旋风式除油器51的内部设有螺旋刮油板52、外壁设有与抽风管32的尾端连通的烟气进口 53、顶部设有与烟气罩41的废气入口 42连通的烟气出口 54,底部与油水收集器55连通,烟气 和含油液滴经抽风管进入油水收集装置5后,含有液滴经螺旋刮油板52与烟气分离,进入油 水收集器55,剩余烟气经烟气出口 54进入下一级烟气罩41,实现石油的回收利用;
[0051] 所述烟气净化装置7的出气管经过抽风机连接至烟囱,将净化达标的废气排出。 [0052]所述的烟气装置4的新风配入口上设有进风管调节阀,通过控制其开度控制新风 的配入量。
[0053]实施例2高含水率含油污泥的综合利用
[0054] 步骤1:将含水率为90%的含油污泥与糠壳、生石灰、生物质炭、氯化铁按质量比 70:5:6:10:9的比例混合制得混合物,所述糠壳的粒径为2mm,所述生物质炭粒径为5mm,发 热量为5000大卡;
[0055] 步骤2:将步骤1所得的混合物送入实施例1所述的负压循环蓄热回收系统的焚烧 装置中,所述混合物的厚度为500腕,混合物的行进速度〇.〇5m/s,点火焚烧,经烟气净化装 置7排出的废气满足欧盟2000标准。
[0056] 实施例3高含水率含油污泥的综合利用
[0057] 步骤1:将含水率为40%的含油污泥与糠壳、生石灰、生物质炭、氯化铁按质量比 80:8:5:3:4的比例混合制得混合物,所述糠壳的粒径为8mm,所述生物质炭粒径为8min,发热 量为4500大卡;
[0058] 步骤2:将步骤1所得的混合物送入实施例1所述的负压循环蓄热回收系统的焚烧 装置中,所述混合物的厚度为700mm,混合物的行进速度〇. lm/s,点火焚烧,经烟气净化装置 7排出的废气满足欧盟2〇〇〇标准。
[0059] 实施例4高含水率含油污泥的综合利用
[0060] 步骤1:将含水率为6〇%的含油污泥与糠壳、生石灰、生物质炭、氯化铁按质量比 60:10:10:10:10的比例混合制得混合物,所述糠壳的粒径为8謹,所述生物质炭粒径为8mm, 发热量为4500大卡;
[0061] 步骤2:将步骤1所得的混合物送入实施例1所述的负压循环蓄热回收系统的焚烧 装置中,所述混合物的厚度为7〇〇mm,混合物的行进速度〇 • 2m/s,点火焚烧,经烟气净化装置 7排出的废气满足欧盟2000标准。
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