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Method for thermal utilization of moist sludge, digestate or agricultural and installation of damp combustion of sewage sludge, digestate or agricultural

机译:湿污泥,消化物或农业的热利用方法以及污水污泥,消化物或农业的潮湿燃烧的安装方法

摘要

a thermal treatment zawilgoconych sewage sludge, pofermentacyjnych or agricultural, in which zawilgocony sludge is to obracanej at from 0.5 to 5 rpm. the engine, in which przesypywany in time from 2 to 10 minutes.towards a window outlet chamber is heated wspu00f3u0142pru0105dowo rotational stream exhaust, characterised by the fact that the drying and pyrolysis zawilgoconego sludge chamber (2) is driven in the rotational atmosphere exhaust stream temperature anaerobic range 700 to 1100u00b0c, 850u00b0c favourably.formed in the chamber (2) karbonizat rotational and ash being drained out is to set up on the bottom of the dyszowym (1.1) fluidalnej combustion chamber (1) of fluid and formed in the revolving chamber (2) zawilgocony pyrolysis gas is made to fluidalnej combustion chamber (1), which is burned after previous mixing with air introduced into the combustion chamber (1) fluidalnej two after ziomach its vertical axisat lower pyrolysis gas is mixed with primary air, doprowadzonym in quantities of from 30 to 50% of the quantity of air required for burning the gas generated stechiometrycznego pyrolysis, and at a higher level of secondary air, doprowadzonym in quantities of from 40 to 60% of the quantity of air required for burning gas stechiometrycznego isolated pizolitycznych.the mixed air zawilgoconego gas pirolitycznego follows from shaped rear wall (1.9) fluidalnej combustion chamber (1), at the height of the window outlet chamber (1), the engine ignition (1.10), warmed up to temperatures of 800 to 900u00b0c spalina the temperature of 900 to 1000u00b0c, arising from the combustion karbonizatu fluidised bed.fluidalnej arising in a combustion chamber (1) gases are routed to the separation chamber (3), and then to pu0142omiennicy (4.1) a waste heat boiler (4), the ash from the combustion chamber (1) fluidalnej is discharged to the discharge of ash (7), and outgoing with a waste heat boiler (4) gases undergo process odpylenia dedusting exhaust system (5), and then cool and dry in the schu0142 adzaju0105co - desiccant unit exhaust gas (6).the subject of the invention is also the thermal utilisation zawilgoconych sewage sludge, pofermentacyjnych or agricultural.
机译:热处理zawilgoconych污水污泥,pofermentacyjnych或农业污水处理厂,其中zawilgocony污泥以0.5至5 rpm的速度运转。发动机,其中przesypywany的时间为2到10分钟。朝着窗户出口室加热wsp u00f3 u0142pr u0105dowo旋转流废气,其特征在于,驱动了干燥和热解的zawilgoconego污泥室(2)旋转气氛排气流的厌氧温度范围最好在700至1100 ,850 u00b0c。在燃烧室(2)中形成旋转并排灰的碳粉应放置在dyszowym(1.1)流体燃烧室的底部( 1)流体并在旋转室(2)中形成,将zawilgocony热解气体送入Fluidalnej燃烧室(1),该流体在预先与引入燃烧室(1)的空气混合后在ziomach的垂直轴下方经过燃烧而燃烧热解气体与一次空气混合,doprowadzonym的量为燃烧生成的化学计量法cznego热解所需要的空气量的30%至50%,且较高的二次空气,doprowadzonym的量为燃烧气体化学计量法所需的空气量的40%至60%cznego孤立的pizolitycznych.zawilgoconego混合气体pirolitycznego的混合空气来自成形后壁(1.9)Fluidalnej燃烧室(1),高度窗户出气室(1),即发动机点火器(1.10)加热到800至900 spalina温度,温度从900至1000 u00b0c温度是由于燃烧室中出现的karbonizatu流化床燃烧.fluidalnej( 1)将气体引导至分离室(3),然后将其送至废热锅炉(4.1)进行除尘(4.1),燃烧室(1)中的灰分被排放到灰分(7)的排放中,然后通过废热锅炉(4)排出的气体经过过程听觉异味症除尘排气系统(5),然后在sch单元中干燥并冷却(6)。本发明的主题是还有热利用zawilg oconych污水污泥,pofermentacyjnych或农业。

著录项

  • 公开/公告号PL233843B1

    专利类型

  • 公开/公告日2019-12-31

    原文格式PDF

  • 申请/专利权人 KARCZ HENRYK;

    申请/专利号PL401288A

  • 发明设计人 HENRYK KARCZ;TOMASZ BUTMANKIEWICZ;

    申请日2012-10-19

  • 分类号F23G5/027;C02F11/12;B09B3;

  • 国家 PL

  • 入库时间 2022-08-21 11:16:45

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