废水设计:排泥设备简介及污泥的深度处理(英文)讲解.ppt

废水设计:排泥设备简介及污泥的深度处理(英文)讲解.ppt

  1. 1、本文档共57页,可阅读全部内容。
  2. 2、有哪些信誉好的足球投注网站(book118)网站文档一经付费(服务费),不意味着购买了该文档的版权,仅供个人/单位学习、研究之用,不得用于商业用途,未经授权,严禁复制、发行、汇编、翻译或者网络传播等,侵权必究。
  3. 3、本站所有内容均由合作方或网友上传,本站不对文档的完整性、权威性及其观点立场正确性做任何保证或承诺!文档内容仅供研究参考,付费前请自行鉴别。如您付费,意味着您自己接受本站规则且自行承担风险,本站不退款、不进行额外附加服务;查看《如何避免下载的几个坑》。如果您已付费下载过本站文档,您可以点击 这里二次下载
  4. 4、如文档侵犯商业秘密、侵犯著作权、侵犯人身权等,请点击“版权申诉”(推荐),也可以打举报电话:400-050-0827(电话支持时间:9:00-18:30)。
查看更多
废水设计:排泥设备简介及污泥的深度处理(英文)讲解

Processing and Treatment of Sludge;目录;Part A;Generalized sludge processing flow diagram;Part B;SLUDGE AND SCUM PUMPING;Other types of pumps such as hydraulic piston slurry pumps have also been used to pump sludge. Chopper pumps are used extensively for pumping scum containing rags, plastics,and other fibrous materials that require shredding. The advantages and disadvantages of each type of pump are summarized in Table 13–14.;Plunger Pumps;The advantages of plunger pumps are as follows:;6. Discharge pressure limitations are approximately 10 to 11 bar (150 to 165 lbf/in.2). (1bar=100kPa) 7. Heavy sludge concentrations may be pumped if the equipment is designed for the load conditions.;Plunger pumps come with one, two, or three plungers (called simplex, duplex, or triplex units) with capacities of 2.5 to 3.8 L/s (40 to 60 gal/min) per plunger, and largermodels are available. Pump speeds should be between 40 and 50 strokes per min.Because grease accumulations in sludge lines cause a progressive increase in head with use, heavier duty pumps should be designed for a minimum head of 6.9 bar (100 lbf/in.2).Capacity is decreased in constant speed pumps by shortening the stroke of the plunger; however, the pumps seem to operate more satisfactorily at or near full stroke. For this reason, many pumps are provided with variable-speed drives for speed control of capacity. A plunger pump differs from a centrifugal or recessed impeller pump in that its discharge is pulsing due to the action of a piston; consequently, the actual flow while sludge is moving in the pipeline is greater than average pumping capacity. The headloss calculations, therefore, must be based on the peak pulsating flow rather than the design flow. The factors given in Table 13–15 can be used to account for the actual peak pulsating or instantaneous flow.;Progressive Cavity Pumps;For example, if a 9.5 L/s (150 gal/min) pump is required the pump selection should be sized for an additional 50 percent or a pump

文档评论(0)

shuwkb + 关注
实名认证
内容提供者

该用户很懒,什么也没介绍

1亿VIP精品文档

相关文档