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1、精选优质文档-倾情为你奉上10万吨糖蜜酒精生产线高浓度有机废水处理项目100,000T molasses alcohol product linehigh concentrated organic wastewater treatment project工艺技术方案Process Technical Design 青岛国桥进出口有限公司（CBC）Qingdao ChinaBridge Imp. & Exp. Co., Ltd（CBC）二OO九 年 四 月第一章 简 介Chapter One Summary我公司投资的10万吨糖蜜酒精，用甘蔗汁为原料产生废糖蜜经过发酵生产酒精，在生产酒精的过程中
2、产生高浓度有机废水。酒精废水未经处理就近排入水体，会造成一定程度的污染，因此，必须建设配套的污水处理设施。The project of 100,000T molasses alcohol product line, use sugarcane juice as raw material to produce sugar cane juice, after fermentation, it produce alcohol. Meanwhile, high concentrated organic wastewater is brought out. If charge the waste wat
3、er without treatment, it will result in pollution. Therefore, the matching waste water treatment is necessary to build.工程规模为日处理酒精废水3372m3 /Project scale: deal with alcohol wastewater 3372 m3 per day.污水处理采用厌氧好氧处理工艺/ The wastewater treatment adopts anaerobic + aerobic process.工程总投资为美元/ The total inves
4、tment is 5,821,400 U.S. dollars.污水处理运行成本为0.225美元/m3。The running cost for wastewater treatment is 0.225 U.S. dollars / m3.第二章 工程规模与处理程度Chapter Two Project scale and treatment level第一节 规模的确定Section one Scale control根据我公司对糖蜜酒精污水处理的治理经验，及厂方提供的数据，确定水量如下：According to the experience on molasses alcohol was
5、tewater treatment and information provided by the factory, the determined water quality is as follows: 糖蜜酒精酒糟水为3372 m3/d（含水93.4%）Molasses alcohol distillers grains water 3372 m3 / d (moisture content 93.4%) 经板框过滤后水量为2300 m3/d。Water quantity after plate and frame filter press is 2300 m3 / d.第二节 进水水质的
6、确定Section two Quality control of inflow water参照同类生产企业的酒精废水参数，及公司确定精废水处理工程的进水水质设计为：CODcr 80000mg/l（板框过滤前） CODcr 45000mg/l（板框过滤后） BOD5 25000mg/l SS 5000mg/l NH3-N 180mg/l PH ： 44.5 T 80Referring to the molasses alcohol parameters of the same type manufacture factories and the determined wastewater val
7、ue, the design is as follows:CODcr 80000mg/l（before plate and frame filter press） CODcr 45000mg/l（after plate and frame filter press） BOD5 25000mg/l SS 5000mg/l NH3-N 180mg/l PH ： 44.5 T 80第三节 污水处理程度的确定Section Three Wastewater treatment level污水处理工程对污水中主要污染物的处理程度是确定处理工艺的基本依据。而处理程度主要依据污水处理厂出水受纳水体的水体标准
8、和环境容量，依照国家颁布的有关排放标准来确定根据中华人民共和国污水综合排放标准（GB89781996），排入该水体的污水执行二级标准，即污水处理站的出水水质应达到：In the wastewater treatment project, the disposal level for the main pollutants in wastewater is the basic criterion to design the process. The disposal level depends on the receiving water body of water standards and
9、environmental capacity. In accordance with the Peoples Republic of Integrated Wastewater Discharge Standard (GB8978-1996), execute the secondary effluent standards for wastewater discharged in the water body, that is, effluent water from wastewater treatment plant should meet the following quality:
10、CODcr 300mg/l BOD5 150mg/l SS 200mg/l PH ： 6-9 NH3N 25mg/l 根据进水水质和出水水质的要求，显然简单的机械处理不能满足要求，因此本工程将采用厌氧好氧生物处理的方式以达到上述要求。According to the requirements of inlet and outlet water quality, apparently simple mechanical processing cannot meet the requirements of this project. Therefore, anaerobic + aerobic p
11、rocess is adopt to meet above requirements.第三章 污水处理工艺的确定Chapter Three Wastewater treatment process第一节 处理工艺选择Section One Treatment process污水处理工艺的选择直接关系到出水水质指标能否达到要求，关系到运行是否稳定可靠，管理是否方便以及投资和运行成本的高低。因此，慎重选择适当的处理工艺是污水处理设计的关键。The choice of wastewater treatment process will directly affect to the outlet wa
12、ter quality, steadily running, management, investment and operation cost. Therefore, careful selection of appropriate treatment technology is the key for wastewater treatment.糖蜜酒精废水是高浓度、高温度的有机废水，因此简单的机械和物化的方法不能保证污水处理的稳定达标排放，高浓度有机废水如果直接进行好氧处理，势必会造成能耗过高，从而增加污水处理的运行成本，而单独的厌氧处理也不能直接达标排放。因此，本污水处理工程采用厌氧+好
13、氧的处理方法。The molasses alcohol wastewater is organic wastewater with high concentration and high temperature. So simple mechanical and physic-chemical method cannot guarantee the qualified discharge of wastewater. If directly use aerobic treatment for high concentrated organic wastewater, it will lead
14、to high cost. And the anaerobic treatment alone cannot reach the requirement either.Therefore, the wastewater treatment project adopts anaerobic + aerobic treatment.一、厌氧工艺的选择 / Anaerobic process目前应用于高浓度废水处理成熟的厌氧方案主要有UASB和BIC,因此针对这两种厌氧工艺进行比较如下：At present, there are two kinds of mature process, UASB a
15、nd BIC, to dispose the high concentrated wastewater. therefore, compare the both processes as follows:（一）UASB厌氧反应器 / UASB anaerobic reactorUASB即为上流式厌氧污泥床反应器，为第二代厌氧反应器的典型代表。整个反应器主体可分为两个区域：反应区和气、液、固三相分离区。污水通过水泵提升到厌氧反应器的底部，利用底部的布水系统将污水均匀地布置在整个截面上，同时利用进水的出口压力和产气作用，使废水与高浓度的厌氧污泥充分接触和传质，将废水中的有机物降解。废水在反应区缓慢
16、上升，进一步降解有机物。气体、水、污泥在同时上升过程中，沼气首先进入三相分离器内部通过管道排出，污泥和废水通过三相分离器的缝隙上升到分离区，污泥在分离区沉淀浓缩并回流到三相分离器的下部，保持厌氧反应器内的生物量，沉淀后的出水通过管道排出罐外。分离区反应区UASB反应器结构示意图出水进水沼气布水系统三相分离器UASB is up-flow anaerobic sludge blanket reactor, it is the typical representative of the second generated anaerobic reactor. The whole reactor ca
17、n be divided into two regions: reaction zone and three-phase separation zone of gas, liquid and solid. Upgrade the wastewater to the bottom of anaerobic reactor by water pump, distribute the wastewater on the whole section by use of water distributor, meanwhile, utilize the outlet pressure and aerog
18、enesis to make wastewater and high concentrated anaerobic sludge have enough contact and mass transfer, and finally degrade the organic matter in wastewater. The wastewater slowly rise in the reaction zone and further degrade the organic compounds. In the ascent process of gas, water and sludge, the
19、 biogas first enter the three-phase separator and then discharge through pipeline, meanwhile, the sludge and wastewater upgrade to the separation zone through the gap. The sludge concentrate and return back into the down part of three-phase separator to keep the biomass in anaerobic reactor, and the
20、 water after precipitation drainage through pipe.（二）BIC厌氧反应器 / BIC anaerobic reactorBIC为我公司自主开发研究的内外双循环厌氧反应器，代表了当今厌氧反应器的最高水平。它是由布水器、提升装置、三相分离器、气液分离器、罐体及出水系统等组成。BIC is internal and external double loops anaerobic reactor, researched and developed by our own company. It represents the highest level of
21、 present anaerobic reactor, composed by water distributor, upgrading device, three-phase separator, gas-liquid separator, tank, water discharge system, etc.可以理解BIC是由上、下两个UASB组成的两个反应室，下反应室负荷高，上反应室负荷低，在反应器内部，对应分为三个反应区。That is, the BIC is two reactors composed by upper and lower UASB. The lower reactor
22、 has high load and the upper reactor has lower load. Inside the reactor, there are three reacting areas.沼气bi进水BIC反应器结构示意图出水分离区精处理区高负荷区布水系统提升装置三相分离器气液分离器高负荷区：借助于本公司的专利防堵塞的布水系统，高浓度的有机废水均匀进入反应器底部，完成与反应器内污泥的充分混合，由于内循环作用、高的水力负荷和产气的搅动，导致反应器底部的高浓度的颗粒污泥呈良好的流化状态，使废水与污泥能够充分接触，如此良好的传质作用和较高的污泥活性保证了BIC反应器具有较高的有机
23、负荷和有机物去除率。 High-load area: With the companys patented anti-clogging water distribution system, high concentrated organic wastewater enters into the bottom of reactor, carry out the fully mixed with sludge. Due to the internal cycle affection, high water load and gas stirring, the high concentrated g
24、ranular sludge is in good flow status, the wastewater and sludge will fully contact. Therefore, good mass transfer and high sludge activity ensure the organic load and removal rate for BIC reactor. 低负荷区：低负荷区也是精处理区，在这个反应区内水力负荷和污泥负荷较低，因此可以有效的对废水中的有机物进行精处理。 Low load area: It is polishing unit, in which
25、 area, the hydraulic load and sludge load is lower. So the organic matter will be effectively removed from the wastewater.沉降区： BIC反应器顶部为污泥沉降区，有机物已基本去除，废水中的少量悬浮物在本区内进一步进行沉降，保证BIC出水水质。 Settlement area: The top area of BIC reactor is settlement area. The organic matter has been basically removed and sm
26、all amount suspended matter in wastewater will have further settlement, which ensures the BIC outlet water quality.基本原理：废水通过布水系统进入厌氧反应器的下部高负荷区，与颗粒污泥进行充分的混合和传质，将废水中大部分的有机物分解，产生大量的沼气。沼气通过提升装置时，由于沼气的提升作用，沼气连同一部分混合液被提升到罐顶部的气液分离器，沼气在气液分离器里被分离出来，分离后的混合液再通过回流管回流到罐的底部，与进入BIC厌氧反应器的进水混合，形成了厌氧罐自身的内循环。 Basic pr
27、inciple: The wastewater enters into the high load area in anaerobic reactor bottom through water distribution system. The wastewater and granular sludge have adequate mixture and mass transfer, upgrade the organic matter and bring out biogas. The biogas and part of the mixed liquor is taken up to th
28、e gas-liquid separator, where the biogas is separated and the mixed liquor reflows to the tank bottom and blend with the inlet water of BIC anaerobic reactor. It forms the self internal circle of anaerobic tank.废水通过提升装置后进入上部低负荷区（精处理区），进一步降解废水中的有机物，混合液通过上部的三相分离器时进行颗粒污泥、水、沼气的分离，沼气通过沼气管道排出，污泥则回流到厌气罐底部保
29、持生物量，而沉淀后的水通过出水堰进入后续构筑物。The wastewater gets into the up part low load area to degrade the organic matter for further. The mixed liquor separates the granular sludge, water and biogas by three-phase separator. The biogas discharge from the biogas pipe and the sludge reflow to the anaerobic tank botto
30、m to keep the biomass.BIC运行成功的关键因素是必须用颗粒污泥接种，以下是我公司在工业废水中培养的颗粒污泥。颗粒污泥照片The key for BIC running is using granular sludge to inoculate. The below is granular sludge brought up by our company.（三）厌氧方案的确定/ Anaerobic plan针对以上这两种厌氧工艺的进行比较，可得结论如下：Compare above two anaerobic plans, thus, achieve below conclu
31、sion”工 艺 方 案 比 较 表指 标 / TargetBICUASB容积负荷a / Capacity load a15-30kgCOD/ m3.d3-8kgCOD/ m3.d运行成本 / Running cost低 / Low低 / Low占地面积b / Site size b少/Small大/Large毒性抑制力c / Virulence restraint c大/Large小/Small耐负荷冲击d / Impact load resistance d强/Strong弱/ Weak布水均匀性e/ Homogeneity of water distribution e均匀/Yes不均匀
32、/No维护与操作 / Maintenance and operation简便/ Easy精心/ Detailed二次污染 / Secondary pollution无/ No无/ No副产品 / Byproduct颗粒污泥和沼气Grain sludge and biogas沼气/ Biogas上升流速f / Ascend speed f10m/h1m/h进水管道的堵塞g/ Block of water inlet pipe g不会/ No会/ Yes注： BIC反应器的有机负荷是UASB反应器有机负荷的4-8倍，UASB反应器的有机负荷通常为3-8kgCOD/ m3.d，而BIC反应器的有机负
33、荷可达到15-30kgCOD/ m3.d。Note: The organic load of BIC reactor is 4-8 times of UASB reactor. The organic load of UASB reactor is usually 3-8kgCOD / m3.d, while the BIC reactor is up to 15-30kgCOD / m3.d. 因BIC有机负荷比UASB高，因此处理同样规模的有机废水，BIC反应器的容积比UASB小，故BIC反应器的占地面积低。 As for the organic load, the BIC is high
34、er than UASB, thus, treating the same capacity wastewater, the volume of BIC reactor is smaller than UASB. In another word, the BIC reactor will take smaller room. 废水中的CL-、SO42-等可能会对厌氧处理有毒性。在UASB中污泥与废水混合不匀，将导致部分污泥受到毒性抑制；而在BIC反应器内，由于大的内循环作用使污泥与废水充分混合，能最大程度的释稀可能的毒性，降低其抑制作用。 The CL- and SO42- in wastew
35、ater may be harmful to the anaerobic treatment process. In the UASB, uneven mixture for sludge and wastewater will lead to toxic inhibition for part of sludge. But in the BIC reactor, big internal circle result in the fully mix for sludge and water, which will crack the toxic as possible and reduce
36、the inhibitory effect. 进水浓度的突然增加或进水量的突然加大，都会对厌氧反应器造成负荷冲击，BIC因其内循环作用，瞬间的高浓度废水进入反应器后，产气量大，气提量会随着增大，从而内循环量大，大的内循环量能将高浓度的废水迅速的释稀，从而减少了有机负荷变化对反应器的冲击。UASB反应器则不然，有机负荷突然增大后，迅速增加的产气量会将污泥带出反应器，严重时会造成恶性循环，导致整个反应器失败。 The sudden increase for inlet water concentration or capacity will result in load impact for th
37、e anaerobic reactor. Because of the internal circle action, at the moment of wastewater entering the BIC, the gas output will increase. The big circulating load will dilute the high concentrated wastewater quickly and reduce the impact to the reactor. The UASV reactor is different. When the organic
38、load suddenly increased, the increased gas output will bring sludge out of the reactor. Seriously, it will cause vicious circle or failure for whole reactor. 高的水力负荷和多旋流式的布水能最大程度的保证布水均匀，UASB大多采用的是多点式布水，并且水力负荷较低，因此布水均匀性不如BIC。 High hydraulic load and multi-cyclone water distribution will maximum ensure
39、 the equally water distribution. The UASB mostly use multipoint water distribution, which has low water load. Therefore, the BIC is better than UASB. 因为内循环的原因，BIC上下反应区具有不同的水力负荷，下反应区具有较高的上升流速，保证了废水与污泥的传质与混合，而上反应区的较低的上升流速，又保证了污泥的沉降不会受到大的影响，UASB反应器的上升流速大于1m/h时，会极易造成污泥的流失。 Because the reasons of cycle,
40、BIC reaction zone has different hydraulic load for upside and downside. The downside has higher up flow rate, ensuring the mass transfer and mix for wastewater and sludge. The upside has lower up flow rate, ensuring the sludge settlement without huge affect. If the up flow rate if UASB reactor excee
41、ds 1m/h, the sludge will lose. BIC多旋流式布水采用了少量的大口径布水管，出口流速可以达到3-5m/s以上，可以有效的防止结垢和堵塞。 BIC cyclone water distribution adopts large-diameter pipes, with the flow rate over 3-5m/s. It can effectively prevent fouling and plugging. 根据上述的工艺比较，结合废水从生产车间的流量、水质不稳定，对废水处理设施冲击大的特点，选用BIC厌氧反应器作为厌氧处理工艺。According to
42、above comparison, combined with instability of wastewater flow volume and quality, as well as the big impact on the water treatment facilities, select BIC anaerobic reactor as anaerobic treatment process.二、好氧工艺方案的选择 / Aerobic process酒精废水中含有大量的蛋白质类物质，这些物质经厌氧分解后转化为氨氮。因此，厌氧出水中含有浓度较高的氨氮，故后续的处理不能采用常规工艺，须
43、用带有脱氮功能的工艺。 本工程中采用A/O法作为好氧脱氮处理工艺。The alcohol wastewater contents a lot of protein matter, which will transfer into NH-N after anaerobic decomposition. Therefore, the outlet water of anaerobic process contents high concentrated NH-N. That means, the following treatment shall not adopts routine proces
44、s but process with denitrifying function. This project use A/O technique to denitrify the N.第二节 工艺方案的确定Section Two Process plan一、工艺流程 / Process flow综上所述，确定本污水处理工艺为厌氧采用BIC厌氧反应器，好氧采用A/O活性污泥法。In sum, the wastewater treatment process determines to use BIC reactor for anaerobic and A/O active sludge proc
45、ess for aerobic.废水处理工艺流程图见附件：The wastewater treatment flow chart is as attached file.二、工艺简介/ Process brief车间过来的酒糟水含有大量的糟渣，首先进入脱水机房进行脱糟处理，脱出来的糟渣外运。There are many grains contained in spent wash from the workshop. First carry out the dehydration proposal and then out transport the slag.脱糟后的废水自流进入调节池，调节
46、废水的水质水量等，然后通过提升泵到BIC，同时进入BIC的还有一沉池回流水，在BIC内利用厌氧菌将废水中的有机物分解成甲烷、二氧化碳等气体，去除废水中的大部分有机物。The wastewater flow to the regulate pond to adjust the water quality and quantity. Then it is pump to the BIC, as well as the reflow water from the first sedimentation tank. In the BIC, the anaerobic organism degrade
47、the organic matter into CH4, CO2 and other gas. Most of the organic matter is released.经过厌氧反应器（BIC）处理后的水自流到一沉池，一沉池出水一部分回流到BIC，剩余的水进入接触氧化池把水中大部分有机物去除，出水进入后续的A/O池，在A/O池内的好氧微生物将废水中剩余的有机物氧化分解，同时将大部分氨氮转化为氮气去除，氧化池出水自流到二沉池，二沉池沉淀的污泥一部分回流到A/O池，上清液达标排放。Water out of the anaerobic reactor ( BIC ) treatment partly flows to the first sedimentation, the first sedimentation water outlet partly reflow to the BIC, the other water enters the contact oxidation pool to remove mo