CN2878390Y - 多功能全自动远程恒温供热废旧轮胎裂化装置 - Google Patents

多功能全自动远程恒温供热废旧轮胎裂化装置 Download PDF

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CN2878390Y
CN2878390Y CNU2006200827316U CN200620082731U CN2878390Y CN 2878390 Y CN2878390 Y CN 2878390Y CN U2006200827316 U CNU2006200827316 U CN U2006200827316U CN 200620082731 U CN200620082731 U CN 200620082731U CN 2878390 Y CN2878390 Y CN 2878390Y
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inner barrel
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王新明
牛斌
窦利德
赵国威
王富昌
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JINAN ECO-ENERGY TECHNOLOGY Co Ltd
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王新明
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Priority to US12/296,181 priority patent/US8168839B2/en
Priority to EP06752931A priority patent/EP2006355A4/en
Priority to AU2006341751A priority patent/AU2006341751B2/en
Priority to KR20087027247A priority patent/KR101183094B1/ko
Priority to CN2006800523991A priority patent/CN101484551B/zh
Priority to PCT/CN2006/001282 priority patent/WO2007115443A1/zh
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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
    • C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
    • C10B53/07—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of solid raw materials consisting of synthetic polymeric materials, e.g. tyres
    • 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
    • C10G1/10—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal from rubber or rubber waste
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/04—Disintegrating plastics, e.g. by milling
    • 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
    • C10B47/00—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion
    • C10B47/28—Other processes
    • C10B47/30—Other processes in rotary ovens or retorts
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/04—Disintegrating plastics, e.g. by milling
    • B29B2017/0424—Specific disintegrating techniques; devices therefor
    • B29B2017/0496—Pyrolysing the materials
    • 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
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1003—Waste materials
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    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/141—Feedstock
    • Y02P20/143—Feedstock the feedstock being recycled material, e.g. plastics
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00—Technologies for solid waste management
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Abstract

本实用新型公开了一种多功能全自动远程恒温供热废旧轮胎裂化装置，属于裂化装置，该裂化装置主要由外筒体和内筒体构成，外筒体静止固定在支座上，内筒体通过传动机构在外筒体内旋转，内筒体的前端设置有贮料器和自动送料器，其后端的上方设有油气出口，下方设有出料口。本实用新型的多功能全自动远程恒温供热废旧轮胎裂化装置和现有技术相比，具有运行平稳、安全、可靠、高效，无任何污染，工艺操作简单，设备寿命长，可实现生产过程的连续化和自动化，转化率高，油品及炭黑质量好，投资小，运行成本低，经济效益显著等优点。

Description

多功能全自动远程恒温供热废旧轮胎裂化装置
技术领域
本实用新型涉及一种将废旧轮胎转变为液体燃料油和炭黑的装置，具体地说是多功能全自动远程恒温供热废旧轮胎裂化装置。
背景技术
随着汽车工业的迅猛发展，废旧轮胎的生成量也越来越多。据世界环境卫生组织统计，世界废旧轮胎积存量已达30亿条，并以每年约10亿条令人惊诧的数字增长。大量的废旧轮胎对环境造成的危害已使人们感到十分忧虑，各个国家及地区的政府部门都在致力于寻求最为理想的处理办法。利用废旧轮胎的裂化以制取清洁油品和炭黑是目前最有效的处理手段。但是，在欧美等工业发达国家，由于技术复杂、装置庞大、投资额巨大以及油品和炭黑质量不合格，不能成为商品，没有经济效益，投入产出比失衡。因此，关于废旧轮胎裂化技术，在这些国家已无生产，处于停滞状态。
发明内容
本实用新型的技术任务是针对以上不足之处，提供一种结构简单、成本低、效率高、对环境无污染的多功能全自动远程恒温供热废旧轮胎裂化装置。
本实用新型解决其技术问题所采用的技术方案是：该裂化装置主要由外筒体和内筒体构成，外筒体静止固定在支座上，内筒体通过传动机构在外筒体内旋转，内筒体的前端设置有贮料器和自动送料器，其后端的上方设有油气出口，下方设有出料口。
外筒体的前端设有导热介质入口，后端设有导热介质出口，并且外表面包覆有保温层；内筒体和外筒体均设置成为前端高、后端低的状态；外筒体和内筒体之间的空腔内充有导热介质。
本实用新型的多功能全自动远程恒温供热废旧轮胎裂化装置和现有技术相比，具有设计合理、结构简单、易于加工、体积小、使用方便、一物多用等特点。
经破碎后的废旧轮胎橡胶块和适量催化剂自动连续加入贮料器，再由自动送料器自动连续送入连续转动的内筒体内。内筒体内的裂化物料由于重力作用，在自前往后移动的过程中，与催化剂充分混合的同时，不断的吸收热量进行低温解聚裂化反应。裂化油气从油气出口不断排出，经外置的冷凝器冷却后成为燃料油，再经进一步分馏、调和后，可得达标汽油和柴油馏分。而解聚裂化彻底完成后剩余的残渣-粗炭黑，从出料口排出，再经炭黑还原处理系统，加工成为合格的炭黑产品。
解聚裂化反应所需热量由远程恒温供热系统提供。热量由导热介质入口进入内、外筒体之间，进一步将热量传递给被裂化物，使其充分解聚裂化。而且对温度的调节和控制，既迅速又精确。
该解聚裂化装置可谓一种性能非常优良的裂化装置，其主要特点表现在：
(1)加热方式独特而先进。由于在废旧轮胎裂化领域采用了远程恒温供热方式，能同时实现“动态加热”和“动态受热”两种状态。所以，使裂化性能、转化率、温度控制和调节、生产率、热效率、油品和炭黑质量、操作安全性、环保性和设备寿命以及经济效益的提高等，均达到最为理想的境界，进入最佳状态。
(2)裂化工艺先进。由于采取的加热方式属于“动态加热”、“动态受热”，所以无需太高的加热温度，就能达到完全的解聚裂化，故而形成了与众不同的最为先进的低温解聚裂化工艺。
(3)可实现对温度的快速而精确的调节和控制，能耗低；
(4)转化率高，可达98％以上；
(5)油品和炭黑质量好。
上述加热方式在相对较低的温度下，就可快速而均衡地将热量传导到被裂化物的所有部位，达到完全的解聚裂化。所以，气态产物收率低，油品收率高，炭黑不会内燃，炭分含量少，质量好。油品、炭黑等产品均可全部变为商品，经济效益显著。
(6)整套工艺装置的操作在全封闭状态下进行，无杂质进入，并无裂化气、液及粉尘泄露，产品质量及安全均有保证。
(7)装置设计完善，结构严密、合理，运行平稳、安全可靠、高效，不会产生任何污染，可完全达到发达国家对安全和环保方面的严格要求。全套装置处理程序简单、操作全部自动化，可降低大量人工费用。
(8)装置投资小，运行成本低，经济效益好。
附图说明
下面结合附图对本实用新型进一步说明。
附图为多功能全自动远程恒温供热废旧轮胎裂化装置的结构示意图。
图中：1、外筒体，2、导热介质入口，3、内筒体，4、传动机构，5、贮料器，6、自动送料器，7、支座，8、出料口，9、油气出口，10、导热介质出口。
具体实施方式
参照说明书附图对本实用新型的多功能全自动远程恒温供热废旧轮胎裂化装置作以下详细地说明。
本实用新型的多功能全自动远程恒温供热废旧轮胎裂化装置，该裂化装置主要由外筒体1和内筒体3构成，外筒体1静止固定在支座7上，内筒体3通过传动机构4在外筒体1内旋转，内筒体3的前端设置有贮料器5和自动送料器6，其后端的上方设有油气出口9，下方设有出料口8。
外筒体1的前端设有导热介质入口2，后端设有导热介质出口10，并且外表面包覆有保温层；内筒体3和外筒体1设置成为前端高、后端低的状态；外筒体1和内筒体3之间的空腔内充有导热介质。
本实用新型的多功能全自动远程恒温供热废旧轮胎裂化装置其加工制作非常简单方便，按说明书附图所示加工制作即可。
除说明书所述的技术特征外，均为本专业技术人员的已知技术。

Claims (4)

1、多功能全自动远程恒温供热废旧轮胎裂化装置，其特征在于该裂化装置主要由外筒体和内筒体构成，外筒体静止固定在支座上，内筒体通过传动机构在外筒体内旋转，内筒体的前端设置有贮料器和自动送料器，其后端的上方设有油气出口，下方设有出料口。
2、根据权利要求1所述的多功能全自动远程恒温供热废旧轮胎裂化装置，其特征在于外筒体的前端设有导热介质入口，后端设有导热介质出口，并且外表面包覆有保温层。
3、根据权利要求1所述的多功能全自动远程恒温供热废旧轮胎裂化装置，其特征在于内筒体和外筒体设置成为前端高、后端低的状态。
4、根据权利要求1所述的多功能全自动远程恒温供热废旧轮胎裂化装置，其特征在于外筒体和内筒体之间的空腔内充有导热介质。
CNU2006200827316U 2006-04-07 2006-04-07 多功能全自动远程恒温供热废旧轮胎裂化装置 Expired - Lifetime CN2878390Y (zh)

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Application Number Priority Date Filing Date Title
CNU2006200827316U CN2878390Y (zh) 2006-04-07 2006-04-07 多功能全自动远程恒温供热废旧轮胎裂化装置
CA 2648504 CA2648504C (en) 2006-04-07 2006-06-12 A continuously cracking technology of waste rubber or plastics and its equipment
US12/296,181 US8168839B2 (en) 2006-04-07 2006-06-12 Continuously cracking technology of waste rubber or plastics and its equipment
EP06752931A EP2006355A4 (en) 2006-04-07 2006-06-12 CONTINUOUS PYROLYSIS PROCESS FOR RUBBER OR PLASTIC WASTE
JP2009503390A JP5187976B2 (ja) 2006-04-07 2006-06-12 廃ゴムやプラスチックの連続熱分解プロセス及び設備
AU2006341751A AU2006341751B2 (en) 2006-04-07 2006-06-12 A continuous pyrolyzing process for waste rubber or plastics
KR20087027247A KR101183094B1 (ko) 2006-04-07 2006-06-12 고무 또는 플라스틱 폐기물 연속 분해 기술 및 장치
CN2006800523991A CN101484551B (zh) 2006-04-07 2006-06-12 一种废旧橡胶或塑料连续裂解工艺及其设备
PCT/CN2006/001282 WO2007115443A1 (en) 2006-04-07 2006-06-12 A continuous pyrolyzing process for waste rubber or plastics

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AU (1) AU2006341751B2 (zh)
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CN101074384B (zh) * 2007-04-28 2010-10-13 牛斌 回转式自动裂解工艺及裂解器

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