CN204892545U - 造纸废弃物资源回收及再利用处理系统 - Google Patents
造纸废弃物资源回收及再利用处理系统 Download PDFInfo
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- CN204892545U CN204892545U CN201520603357.9U CN201520603357U CN204892545U CN 204892545 U CN204892545 U CN 204892545U CN 201520603357 U CN201520603357 U CN 201520603357U CN 204892545 U CN204892545 U CN 204892545U
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- 238000011084 recovery Methods 0.000 title abstract description 5
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- 239000002699 waste material Substances 0.000 claims abstract description 31
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- 239000010802 sludge Substances 0.000 claims description 16
- 238000003860 storage Methods 0.000 claims description 13
- 238000007599 discharging Methods 0.000 claims description 9
- 238000004062 sedimentation Methods 0.000 claims description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound 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- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminum Chemical compound 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Abstract
本实用新型造纸废弃物资源回收及再利用处理系统，其包含垃圾处理系统、水处理站及废气处理系统；其中垃圾处理系统具有储存废弃物的原料坑，原料坑连接撕碎机，撕碎机连接磁选带，磁选带连接摩擦清洗池，摩擦清洗池连接一段漂洗池，一段漂洗池通过摩擦上料机连接脱浆机，脱浆机通过刮料机连接二段漂洗池，二段漂洗池连接脱水机，脱水机通过出料风机连接造粒机；上述撕碎机、摩擦清洗池、摩擦上料机、脱浆机、脱水机均连接水处理站；摩擦清洗池、一段漂洗池、二段漂洗池还连接补充水路；撕碎机、脱水机、摩擦上料机、脱浆机连接冷却水路;造粒机连接废气处理系统。本实用新型完善废纸再生造纸流水线，彻底解决造纸行业废弃物处置的二次污染的问题。
Description
技术领域
[0001] 本实用新型是有关于一种垃圾处理回收再利用处理系统，特别是关于造纸废弃物资源的回收及再利用处理系统。
背景技术
[0002] 随着社会的发展，人民消费水平的提高，人均耗纸量在不断增加，仅靠木材或竹子制浆远远不能满足日益增长的需求。这就需要造纸行业不断地扩大规模，但与此同时其带来的环境问题、生态问题和社会问题不断地突显出来。
[0003]目前，符合循环经济和节能减排要求的废纸回收再利用已经成为制浆工艺的主要来源。但由此也带来了固废污染问题。在废纸再生造纸过程中产生的大量的含塑造纸废弃物，由于成份复杂，处理利用难度大，目前大部份仍然只采取简单的堆放和填埋，不仅占用大量土地，而且极易对水体和空气产生二次污染，并且由于采用汽车运输的方式，不仅粘挂、滴淌、污染环境，而且建设能够容纳大量污泥的大型填埋场基建投资多、占地面积大，再加上企业周边土地资源的日趋紧张，如今这些草渣、污泥等固体废物的出路问题已经是各个制浆造纸企业迫在眉睫急需解决的问题。根据中国造纸行业协会2013年度报告提示，2013年全国造纸企业废纸总消耗量为7401万吨，消耗废纸浆量为5940万吨。由此推算，每年产生的造纸废弃物量约为1461万吨。
[0004]目前，我国对造纸废弃物的处理主要方法是焚烧和填埋，外有一些非法清洗加工回收塑料，违规排放污水废气的民间作坊。焚烧，其代价十分昂贵，设备投资额大、环保执行标准高，为我国一般造纸行业所承担不起，而且还产生大量的废气，易造成大气污染。填埋为普遍采用的方法，由于缺乏资金建立防渗和水质监测系统，土壤资源浪费和地下水资源受污染将越来越严重，已成为我国水污染和土壤污染的主要污染源之一。一些造纸厂为节约成本，随意堆放造纸废弃物，另有非法加工造纸废弃物普遍存在，但这些做法对土壤和水体污染及其严重，是国家环保法规严厉禁止和打击的。严格按照国家倡导的循环经济的实际操作原则，减量化、资源化、无害化处理技术逐步成为解决造纸固体废弃物二次污染和未来我国治理造纸废弃物的发展趋势。
实用新型内容
[0005] 本实用新型所解决的技术问题即在于完善废纸再生造纸流水线，彻底解决造纸行业废弃物处置的二次污染的问题，并对造纸废弃物资源回收及综合利用，不止是回收资源和能源，其最终目标是脱掉造纸业高能耗、重污染的帽子，清洁生产。
[0006] 本实用新型所采用的技术方案为:一种造纸废弃物资源回收及再利用处理系统，其包含垃圾处理系统、水处理站及废气处理系统；其中垃圾处理系统具有储存废弃物的原料坑，原料坑连接撕碎机，撕碎机连接磁选带，磁选带连接摩擦清洗池，摩擦清洗池连接一段漂洗池，一段漂洗池通过摩擦上料机连接脱浆机，脱浆机通过刮料机连接二段漂洗池，二段漂洗池连接脱水机，脱水机通过出料风机连接造粒机；上述撕碎机、摩擦清洗池、摩擦上料机、脱浆机、脱水机均连接水处理站；摩擦清洗池、一段漂洗池、二段漂洗池还连接补充水路；撕碎机、脱水机、摩擦上料机、脱浆机连接冷却水路；造粒机连接废气处理系统。
[0007] 其特征在于，该水处理站设置地沟，地沟与纸浆堆场相连接，地沟与纸浆堆场之间依序设置机械格栅、滚筒筛、有轴螺旋及纸浆输送带；地沟通过滚筒筛连接集水池，集水池经过中间水池连接深层气浮系统，同时，集水池还连接立式碎浆机，立式碎浆机连接纸浆堆场和地沟；深层气浮系统连接沉淀池和清水池，清水池连接补充水路提供循环补充水，沉淀池和深层气浮系统同时汇总至污泥浓缩池。
[0008] 深层气浮系统还连接MBR池，MBR池一方面设有排水管将余水排出，另一方面连接清水箱，清水箱连接冷却水路，作为冷却水的水源。
[0009] 该废气处理系统包含喷淋塔，喷淋塔连接第二地沟，第二地沟连接第二集水池，第二集水池连接气浮系统，气浮系统连接储存池，储存池连接城市污水处理站；气浮系统还连接加药装置，并连接第二污泥浓缩池；储存池连接第二集水池，第二集水池连接第二污泥浓缩池；第二污泥浓缩池连接污泥吨桶；储存池利用提升栗连接喷淋塔。
[0010] 喷淋塔连接补水装置。喷淋塔还通过引风机连接活性炭吸附塔，再连接烟囱。一段漂洗池底部连接鼓风机
[0011] 本实用新型的有益效果为:得到一整套完整的造纸废弃物资源回收再利用系统，其对造纸废弃物的回收、利用、废水及废气处理给出了一套完整的处理方案，解决了现有技术中高能耗、重污染的问题。
附图说明
[0012] 图1为本实用新型的整体系统示意图。
[0013] 图2为本实用新型的水处理站系统示意图。
[0014] 图3为本实用新型的废弃处理喷淋塔的废水处理系统示意图。
具体实施方式
[0015] 如图1-3所示，本实用新型一种造纸废弃物资源回收及再利用处理系统，其总体包含垃圾处理系统、水处理站及废气处理系统。
[0016] 其中垃圾处理系统具有储存废弃物的原料坑1，原料坑I连接撕碎机2，撕碎机2连接磁选带3，磁选带3连接摩擦清洗池4，摩擦清洗池4连接一段漂洗池5，一段漂洗池5通过摩擦上料机6连接脱浆机7，脱浆机7通过刮料机8连接二段漂洗池9，二段漂洗池9连接脱水机10，脱水机10通过出料风机11连接造粒机12。
[0017] 上述撕碎机2、摩擦清洗池4、摩擦上料机6、脱浆机7、脱水机10均连接水处理站
13 ;摩擦清洗池4、一段漂洗池5、二段漂洗池9还连接补充水路14。补充水路可以是后续的循环补充水路，也可以是额外的补充水路。
[0018] 撕碎机2、脱水机10、摩擦上料机6、脱浆机7连接冷却水路15。
[0019] 造粒机连接废气处理系统16。
[0020] 本实用新型所针对的垃圾，主要是造纸废弃物，特别是废纸再生造纸所产生的造纸废弃物，这种造纸废弃物的成分中主要有PP、PE、瓶片、纸浆、铁、铝、工程塑料(ABS、PC、PVC,PS等)、木头、布条、泥沙等。废弃物储存在原料坑中，首先可以经过人工挑选除去体积较大的瓶片、金属片、布条等物质，并可以使用悬挂除铁器Ia除铁。经过人工筛选和除铁机除铁后的原料进入撕碎机，撕碎处理后经磁选带进行磁选，废铁经过废铁输送带3a最终将原料中的废铁除去，废铁装入废铁吨袋3b。除铁后的原料经过摩擦清洗池处理，实现了纸浆与塑料薄膜的分离，产生的大量纸浆随清洗废水进入水处理站。摩擦清洗池的摩擦清洗过程中使用的是摩擦清洗机，这是一种现有的设备。摩擦清洗后，废料继续进入一段漂洗池(漂洗池中的介质为水，主要作用是将摩擦清洗后的原料进行再次漂洗，类似于衣服用洗衣粉洗后需用清水再次漂洗)进行漂洗，同时可以利用鼓风机17将空气由池子底部进入漂洗池中，使清洗的原料(主要成分PP、PE塑料薄膜)根据密度差实现物质的上下分离。密度大于水的重组分(工程塑料、泥沙等)，统称“重渣”，可经过底部螺旋侧排渣口 5a排出，进而通过重渣输送带5b外运处理；密度小于水的PP、PE塑料薄膜和少量重渣分离后通过摩擦上料机，再次去除掉的部分纸浆随废水进入水处理站。剩余物质继续进入脱浆机后送入刮料机并可以经过螺旋上料的方式进入二段漂洗池进行再次漂洗。上料时使用的设备可以为螺旋上料机8a，物料通过螺旋主轴输送到顶端，落下且一直持续循环，从而达到输送物料的目的。脱浆机脱浆过程中产生的部分纸浆和废水一同经地沟进入水处理站。经二段漂洗池处理后产生的重渣同样经过底部螺旋侧排渣口 5a排出，并进行后续处理，如图，可以装入重渣吨袋9a。去除重渣的原料随后经过螺旋出料、脱水机和出料风机处理后即可产生造粒所需的干净原料塑料薄膜。螺旋出料使用的设备为螺旋出料机％，工作原理是物料通过螺旋主轴输送到外部，且一直持续循环，从而达到输送物料的目的。螺旋出料和脱水机中产生的废水进入水处理站进行后续处理。干净的PP、PE塑料薄膜可通过造粒机生产出塑料颗粒，实现了造纸废弃物的资源回收及综合利用。
[0021] 如图2所示，该水处理13站设置地沟18，地沟18与纸浆堆场19相连接，地沟18与纸浆堆场19之间依序设置机械格栅20、滚筒筛21、有轴螺旋22及纸浆输送带23。图中只标出了摩擦清洗池和漂洗池，其并非只限于此两种设施。
[0022] 地沟18通过滚筒筛21连接集水池24，集水池24经过中间水池25连接深层气浮系统26，同时，集水池24还连接立式碎浆机27，立式碎浆机27连接纸浆堆场19和地沟18。
[0023] 深层气浮系统26连接沉淀池29和清水池30，清水池30连接补充水路14提供循环补充水，沉淀池29和深层气浮系统26同时汇总至污泥浓缩池31。
[0024] 深层气浮系统26还连接MBR，32，MBR池32 —方面设有排水管32a将余水排出，另一方面连接清水箱33，清水箱33连接冷却水路15，作为冷却水的水源，并回流至地沟18。
[0025] 整条清洗线上所产生的废水汇集到地沟流经滚筒筛(地沟流经滚筒筛之间可以设有机械格栅可清除大颗粒杂质)，滚筒筛收集得到的大量纸浆即可经过有轴螺旋、纸浆输送带最后送至纸浆堆场。废水继续流至集水池，经过短暂的物理沉淀作用后上方含纸浆较少的污水经过深层气浮系统、沉淀池、清水池处理后可实现废水的循环利用。
[0026] 深层气浮系统的气浮设备是一类在水中通入或产生大量的微细气泡，使空气以高度分散的微小气泡形式附着在悬浮物颗粒上，造成密度小于水的状态，利用浮力原理使其浮在水面，从而实现固-液分离的水处理设备，是现有设备。
[0027] 集水池底部沉淀物质经过水栗提升后进入立式碎浆机，洗浆后产生的纸浆最终运送至纸浆堆场，处理后的污水回流至地沟。集水池上方澄清废水则自流进入深层气浮系统进而通过沉淀池处理产生底泥，最终通过污泥浓缩池即可实现污泥和废水的分离。产生的污泥经过板框压缩实现污泥外运处理，分离出的废水则回流至中间水池和集水池。此外深层气浮系统中部分的污水通过MBR池、清水箱后对脱浆机、脱水机撕碎机的轴承进行冷却后回流至地沟。
[0028] 该废气处理系统16包含喷淋塔34，喷淋塔34连接第二地沟181，第二地沟181连接第二集水池241，第二集水池24连接深层气浮系统261，气浮系统261连接储存池35，储存池35连接城市污水处理站36 ;气浮系统261还连接加药装置37，并连接第二污泥浓缩池311 ;储存池35连接第二集水池241，第二集水池241连接第二污泥浓缩池311 ;第二污泥浓缩311池连接污泥吨桶34 ;储存池35可以利用提升栗39连接喷淋塔34。喷淋塔还连接补水装置，这里的补水装置可以取水自补充水路。喷淋塔34还通过引风机40连接活性炭吸附塔41，再连接烟囱42，再将废气排出。
[0029] 造粒废气通过喷淋塔后产生的废水自流至第二地沟，随后流至第二集水池。第二集水池中废水可以先人工清理，经过人工清理后，浮渣浮油进入第二污泥浓缩池。接着进入气浮系统与加药系统中药物混合产生的浮渣浮油也进入第二污泥浓缩池，第二污泥浓缩池的污泥通过栗提升打到污泥吨桶。气浮系统中处理过的清水流入储存池，多余的清水溢流至第二集水池，其余废水则可通过水栗提升再次进入喷淋系统进行循环利用，多余废水则达标排放。
[0030] 生产塑料颗粒时产生的造粒废气经过喷淋塔进行喷淋可去除烟气中大部分的有害物质，后经引风机进入活性炭吸附塔吸附后达到国家排放标准后经烟囱进行外排。造粒废气在喷淋塔中通过碱液及除味剂43处理后产生大量的喷淋废水进入专门处理喷淋废水的喷淋废水处理站44进行处理后，达标后排放。
[0031] 本案中，各个物料的流动，可以依据需求采用栗、传送带等常规技术手段，在此不再赘述。
Claims (7)
1.一种造纸废弃物资源回收及再利用处理系统，其特征在于，其包含垃圾处理系统、水处理站及废气处理系统； 其中垃圾处理系统具有储存废弃物的原料坑，原料坑连接撕碎机，撕碎机连接磁选带，磁选带连接摩擦清洗池，摩擦清洗池连接一段漂洗池，一段漂洗池通过摩擦上料机连接脱浆机，脱浆机通过刮料机连接二段漂洗池，二段漂洗池连接脱水机，脱水机通过出料风机连接造粒机； 上述撕碎机、摩擦清洗池、摩擦上料机、脱浆机、脱水机均连接水处理站；摩擦清洗池、一段漂洗池、二段漂洗池还连接补充水路； 撕碎机、脱水机、摩擦上料机、脱浆机连接冷却水路； 造粒机连接废气处理系统。
2.如权利要求1所述的造纸废弃物资源回收及再利用处理系统，其特征在于，该水处理站设置地沟，地沟与纸浆堆场相连接，地沟与纸浆堆场之间依序设置机械格栅、滚筒筛、有轴螺旋及纸浆输送带； 地沟通过滚筒筛连接集水池，集水池经过中间水池连接深层气浮系统，同时，集水池还连接立式碎浆机，立式碎浆机连接纸浆堆场和地沟； 深层气浮系统连接沉淀池和清水池，清水池连接补充水路提供循环补充水，沉淀池和深层气浮系统同时汇总至污泥浓缩池。
3.如权利要求2所述的造纸废弃物资源回收及再利用处理系统，其特征在于，深层气浮系统还连接MBR池，MBR池一方面设有排水管将余水排出，另一方面连接清水箱，清水箱连接冷却水路，作为冷却水的水源。
4.如权利要求1所述的造纸废弃物资源回收及再利用处理系统，其特征在于，该废气处理系统包含喷淋塔，喷淋塔连接第二地沟，第二地沟连接第二集水池，第二集水池连接气浮系统，气浮系统连接储存池，储存池连接城市污水处理站； 气浮系统还连接加药装置，并连接第二污泥浓缩池； 储存池连接第二集水池，第二集水池连接第二污泥浓缩池； 第二污泥浓缩池连接污泥吨桶； 储存池利用提升栗连接喷淋塔。
5.如权利要求4所述的造纸废弃物资源回收及再利用处理系统，其特征在于，喷淋塔连接补水装置。
6.如权利要求4所述的造纸废弃物资源回收及再利用处理系统，其特征在于，喷淋塔还通过引风机连接活性炭吸附塔，再连接烟囱。
7.如权利要求1所述的造纸废弃物资源回收及再利用处理系统，其特征在于，一段漂洗池底部连接鼓风机。
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN106077028A (zh) * | 2016-06-20 | 2016-11-09 | 许昌中亚工业智能装备股份有限公司 | 一种造纸废渣回收装置 |
| CN107059450A (zh) * | 2017-05-25 | 2017-08-18 | 山东宇能机械有限公司 | 造纸厂废料纸浆处理工艺 |
| CN107716510A (zh) * | 2017-10-17 | 2018-02-23 | 广东龙跃环境科技有限公司 | 一种造纸厂废渣的处理系统及其处理工艺 |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106077028A (zh) * | 2016-06-20 | 2016-11-09 | 许昌中亚工业智能装备股份有限公司 | 一种造纸废渣回收装置 |
| CN106077028B (zh) * | 2016-06-20 | 2018-02-27 | 许昌中亚工业智能装备股份有限公司 | 一种造纸废渣回收装置 |
| CN107059450A (zh) * | 2017-05-25 | 2017-08-18 | 山东宇能机械有限公司 | 造纸厂废料纸浆处理工艺 |
| CN107716510A (zh) * | 2017-10-17 | 2018-02-23 | 广东龙跃环境科技有限公司 | 一种造纸厂废渣的处理系统及其处理工艺 |
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