青山湖污水处理厂工程优化初步设计

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1、青山湖污水处理厂工程Qing Shan Hu Sewage Treatment Plant优化初步设计Optimized Preliminary Design工号 Proj.No:2002-163中国市政工程华北设计探讨院North China Municipal Engineering Design & Research Institute2003年01月国徽工程设计证书甲级单位名称：中国市政工程华北设计探讨院业务范围：市政公用行业（地铁轻轨除外）甲级、建筑行业建筑工程甲级、冶金行业（焦化）甲级。以下空白证书编号：020010-sj有效期：*发证部门：中华人民共和国建部（印章）2002年7月

2、17日中华人民共和国建设部印制文件签署院 长 曹开朗主 管 副 院 长 徐 强院 总 工 程 师 李成江安排经营部部长 王 起技术质量部部长 李颜强设 计九所 所 长 刘晓松设计九所 副所长 胡永龙设计九所总工程师 申 蓁项 目 负 责 人 申 蓁本人签署页院级审核审定 李成江第九设计所所长 刘晓松第九设计所副所长 胡永龙第九设计所总工 申 蓁项目负责人 申 蓁工艺专业负责人 李 晶总图专业负责人 宫业龙电气专业负责人 刘 清自控专业负责人 余 颖建筑专业负责人 黄玉慧结构专业负责人 刘迎焕暖通专业负责人 李小慧青山湖污水处理厂工程Qing Shan Hu Sewage Treatment P

3、lant优化初步设计Optimized Preliminary Design第一卷设计说明书Part One:Specification of Optimized Design目 录Content前言Preface-011 设计依据Bases of Design-2 设计范围Design Scope-3 工程规模Scale of the Project-4 污水处理厂进水水质Raw sewage quality of Qing Shan Hu Sewage Treatment Plant-5 污水处理厂出水水质Effluent quality of Qing Shan Hu Sewage Tr

4、eatment Plant-6 污水处理厂处理工艺Treatment Process of the Sewage Treatment Plant-7 污水处理厂工程设计Engineering Design of Sewage Treatment Plant-7.1工程内容Engineering Content-7.2处理单元工艺设计Design of Treatment Process Unit-7.3总平面设计General Layout-7.4高程设计Design of Altitude-7.5附属设施Other Facilities-7.6建筑设计说明Notes For Architec

5、ture-7.7结构设计说明Structure Design Reference-7.8电气设计Electrical Design-7.9自动化仪表及限制系统的设计Automatic Control System And Instrumentation Design-8 暖通设计HV & AC Notes-9人员编制Staff Arrangement-前言Preface中国市政工程华北设计探讨院受德国柏林水务国际有限公司的托付，对南昌市青山湖污水处理厂工程进行施工图阶段设计。North China Municipal Engineering Design & Research Institut

6、e is commissioned by Berlinwasser International GmbH to the construction design of the Qing Shan Hu Sewage Treatment Plant in Nanchang city.在此之前德国柏林水务国际有限公司依据已审批的江西省南昌市青山湖污水处理工程初步设计提出了初步设计优化方案设想，并通过了有关方面的审查论证。为此，在施工图设计之前，中国市政工程华北设计探讨院需以柏林水务国际有限公司提出的初步设计优化方案设想为基础并充分体现柏林水务国际有限公司的宗旨，对原江西省南昌市青山湖污水处理工程初步

7、设计进行修改即优化初步设计。双方就工程技术方案进行了仔细探讨、沟通、磋商形成共识后，我院于2002年12月15日起先了本项目的初步设计优化设计工作，于2003年1月23日完成。在文件的编制过程中，得到了柏林水务国际有限公司的专家的大力支持和协作，同时也得到了南昌市污水处理工程有限公司等有关部门的支持和帮助。Berlinwasser International GmbH had put forward the conception of optimized preliminary design according to the audited “Preliminary Planning of N

8、anchang City Qing Shan Hu Sewage Treatment Plant in Jiangxi Province” which has passed through the audit. Therefore, the optimizing of preliminary design of NCMEDRI should be based on the conception of optimized preliminary planning and the accomplished preliminary design, and take full consideratio

9、n of the tenet of the Berlinwasser International GmbH. After a thorough discussion NCMEDRI start to work at 12.15.2002, and completed at 01.23.2003. During compiling, NCMEDRI received great help and support from Berlinwasser International GmbH and Nanchang Sewage Treatment Company.本文件由三部分内容组成： 第一卷 优

10、化初步设计说明书其次卷 主要设备材料清单第三卷 设计图纸The whole document is composed of three parts:Part One: Specification of Optimized DesignPart Two: Main Equipments and Material ListPart Three: Design Drawings在第一卷中我们只对污水处理厂的工程设计部分做简要说明，其余方面可参见原初步设计，在本文件中不重复累述。Only a brief description of the engineering design of the sewa

11、ge treatment plant will be done in Part One, and others can be referred to in the original preliminary design, therefore, it will not be repeated here.1 设计依据Bases of Design江西省南昌市青山湖污水处理厂工程初步设计说明书及图纸（上海市政工程设计探讨院）（南昌市城市规划设计探讨总院）2002年4月“Specification of the Preliminary Design for Nanchang City Qing Sha

12、n Hu Sewage Treatment PlantProject” and corresponding drawings (Shanghai Municipal Engineering Design & Research Institute) (Nanchang General Urban Layout Design and Research Institute)施工图设计合同Construction Design Contract南昌市青山湖污水处理厂初步设计优化方案（柏林水务国际有限公司）Strategy of Optimized Preliminary Design for Nanc

13、hang City Qing Shan Hu Sewage Treatment Plant (Berlinwasser International GmbH)南昌市青山湖污水处理厂优化设计备忘录（2002年12月13日）Notes of optimizing design for Nanchang City Qing Shan Hu Sewage Treatment Plant (12.13.2002)2 设计范围Design Scope本项目的设计范围为青山湖污水处理厂工程（围墙内）。对厂内的工艺、建筑、结构、总图、电气、自控、暖通进行优化设计。Area for which design i

14、s to be performed: Complete sewage treatment plant premises up to the perimeter fence (inclusive): including optimizing of process, architecture and civil engineering, general drawing, electric & automatic control, and heating & ventilation.3 工程规模Scale of the project依据污水量预料，青山湖污水处理厂最终规模99万m3/d，分三期建设

15、，一期规模33万m3/d。本项目按一期规模设计，充分考虑与二、三期的连接。According to the prediction of the flow quantity, Qing Shan Hu Sewage Treatment Plant, Nanchang, consisting of the mechanical treatment stage (990,000m3/d) and the biological treatment stage (330,000m3/d). The design work is based on the scale of 330,000m3/d and

16、take full consideration of the further two stages.4 污水处理厂进水水质Raw sewage quality of the sewage treatment plant确定青山湖污水处理厂进水水质为：Raw sewage quality of Qing Shan Hu Sewage Treatment Plant is as the following:CODcr 250mg/LBOD5 130mg/LSS 200mg/LNH3-N 20mg/L磷酸盐Phosphate（以P计calculated as P）2.0mg/L依据排水协议，无需考虑

17、水质波动。No fluctuation of water quality need be considered according to the Supply Agreement.5 污水处理厂出水水质Effluent quality of Qing Shan Hu Sewage Treatment Plant青山湖污水处理厂出水水质如下：Effluent quality of Qing Shan Hu Sewage Treatment Plant is as the following:CODcr 120mg/LBOD5 30mg/LSS 30mg/L磷酸盐Phosphate（以P计calc

18、ulated as P）1.0mg/LNH3-N 25mg/L6 污水处理厂处理工艺Treatment Process of the Sewage Treatment Plant依据德国柏林水务国际有限公司的初步设计优化方案，青山湖污水处理厂处理工艺如下：According to the strategy of optimized preliminary design of Berlinwasser International GmbH, the treatment process will be as the following:污水处理工艺采纳普曝法工艺。曝气池为氧化沟形式，采纳表面曝气机

19、曝气。Traditional aeration process will be applied in the treatment. The oxidation ditches are adopted as aeration tanks with upside-down surface aerators.污泥处理工艺采纳厌氧中温消化，消化后的污泥经机械脱水后外运。Anerobic mild temperature digestion is adopted in the treatment of sludge, and digested sludge shall be transported ou

20、t after mechanical dewatering.对消化过程中产生的沼气进行综合利用，其用途有The usage of the biogas produced during digestion:（1） 用于拖动进水泵的沼气发动机To drive the 2 screw pumps.（2） 用于加热消化池的沼气锅炉To heat up the digestion tank through biogas boiler:（3） 用于厂区综合楼的集中空调溴化锂机组To the lithium bromide unit for central air-conditioning in the g

21、eneral office building.沼气利用的气量及热量平衡图见污泥处理工艺设计部分The amount and heat balance chart of the biogas please refer to the process design of sludge treatment.青山湖污水处理厂处理工艺流程如下：The flow of the Qing Shan Hu Sewage Treatment Plant is as the following: 雨水溢流 栅渣外运 栅渣外运 计量 原污水曝气沉砂池细格栅站粗格栅及进水泵房 计量终沉池低排沟氧化沟污泥脱水机房储泥池消

22、化池污泥浓缩机房污泥缓冲池 污泥泵池沼气利用沼气柜泥饼外运7 污水处理厂工程设计Engineering Design of the Sewage Treatment Plant7.1 工程内容Engineering Content青山湖污水处理厂规模33万m3/d，并予留二、三期规模发展用地，其主要内容包括：The design scale Qing Shan Hu Sewage Treatment Plant is 330,000m3/d, and the developing area for further second and third stage is left. Main con

23、tent is set as below:污水提升与预处理系统Sewage pumping and pretreatment system污水生化处理系统Sewage biological treatment system污泥处理系统Sludge treatment system厂区附属建筑Other buildings in plant厂区动力系统（包括变配电系统）Power system in plant (including transformer system)自动限制监测仪表系统Automatic control and instrument system厂区总平面及配套设施Gene

24、ral layout of the plant and supporting system7.2 处理单元工艺设计Design of treatment process unit设计规模Q=33万m3/dScale: Q=330,000m3/d依据要求，截流倍数为2的雨水经污水处理厂预处理后（经曝气沉砂后）干脆溢流至厂区南侧的低排沟。Rain water whose interception multiple is 2 overflows to Dipai trough in front of the south of the plant after pretreatment (aeratio

25、n grit chamber)雨季最大设计流量Qmax=11.46 m3/s(Qmax=990000 m3/d)The Rain season Qmax=11.46 m3/s(Qmax=990000 m3/d)旱季最大设计流量Q旱max=4.40 m3/s(Q旱max=380000 m3/d)The dry season Q旱max=4.40 m3/s(Q旱max=380000 m3/d)旱季平均设计流量Q平均=3.82 m3/s(Q平均=330000 m3/d)The dry season Q平均=3.82 m3/s(Q平均=330000 m3/d)(1) 粗格栅及进水泵房Coarse sc

26、reen and inlet pump station设计参数及描述：Design parameters and description粗格栅及进水泵房土建及设备规模均按一期规模设计并充分考虑与二、三期规模的连接。Scale of civil Engeneering and equipments are set forth according to the first stage and give full consideration to the further second and third stage.设计流量：雨季最大流量Qmax=11.46 m3/sDesign flow quan

27、tity:Rain season Qmax=11.46 m3/s 旱季最大流量Q旱max=4.40 m3/s Dry season Q max=4.40 m3/s旱季平均流量Q平均=3.82 m3/sDry season Q aver. =3.82 m3/s粗格栅间的设置，可去除污水中较大漂移物以保证污水提升泵的正常运行，粗格栅间内安装有齿耙除污机和用于修理的闸门等设备。该格栅除污设备带有独立轨道及抓爪，依据时间间隔或格栅前后水位差，自动启闭悬挂在载重滑车上的机械抓爪，将污物排放至收集箱，完成栅渣的收集、输送和装箱。采纳机械格栅与进水泵房合建，共设三条渠道，单沟宽2000mm，正常状况下，三台

28、格栅运行，事故时互为备用。Coarse screen is designed to remove the relative big floaters to ensure the normal operation of the inlet pump. Rake and maintenance gates etc are installed in the coarse screen station. Rake brings itself independent trails and grippers, and remove the screens to the dustbin automatica

29、lly according to time intermittent or water level difference. It accomplishes the collection, transportation and incasement. The coarse screen and inlet pump station are joined together. There are altogether 3 channels designed in the coarse screen station with individual width 2000mm. 3 coarse scre

30、ens are in operation normally and be standby by each other when accidents happen.设置进水泵房，用来提升污水以满意后续污水处理流程及竖向的连接要求，为地下式钢筋混凝土矩形集水池，泵房与粗格栅合建，污水经泵房提升后通过渠道，进入细格栅站。进水泵采纳螺旋泵型式，以提高效率削减维护。内设6台螺旋污水泵，旱季3用3备，雨季6台全开。依据沼气平衡计算，其中两台进水泵采纳沼气发动机驱动，当运行初期无沼气时可用自然气短暂替代。依据实际运行状况租用自然气子站用专用车。每台螺旋泵前均设有闸门以便检修。在集水泵池上部建有泵房，用于防护

31、螺旋泵的电机和沼气发动机及配套的余热利用系统，室内装有现场电控柜及PLC柜。The inlet pump station is designed for pumping sewage to satisfy the treatment flow and vertical link up. It is an underground reinforced concrete rectangular tank, will be built together with the coarse screen. Sewage is pumped to the fine screen station throug

32、h channels. 6 screw pumps are adopted to improve efficiency and reduce maintenance. 3 are in operation and three standby in dry season and 6 in operation in rain season. 2 of the 6 screw pumps are drove by biogas engines due to the balance calculation of the biogas. In the first period of operation

33、when there is not enough biogas, the 2 biogas engines will use natural gas as fuel. Special trucks will be leased from the natural gas substation according to operation requirement. A rectangular gate is set before each of the screw pump for its maintenance. A pump house is built on the channels in

34、which are engines for screw pumps, heat recycling systems and PLC & control panels.粗格栅间尺寸： 长X宽X高 7m x 8m x 5.8mDimensions of the coarse screen: Length x width x heigh 7m x 8m x 5.8mB. 主要设备及参数Main equipments and parameters齿耙除污机Rake数量： 3套Quantity: 3 sets格栅宽度：B=2.0mWidth of the screen: B=2.0m栅条间隙：b=80m

35、mClearance of the bars: b=80mm栅条倾角：=70oInclination of the bars: =70o栅前水深：2.25m（雨季）Water depth before screen: 2.25m(rain season) 1.47m（旱季最大）1.47m (max.in dry season) 过栅流速：0.65m/s 旱季流速velocity : 0.65m/s(Dry season)1.0m/s雨季流速1.0m/s (rain season)电动闸门数量： 3套Quantity: 3 sets规格： 2m x 1.8m N=2.2kwSpecificati

36、on: 2m x 1.8m N=2.2kw螺旋泵及配套设备Screw pumps and its accessories设备数量：6 套（雨季全开，平均旱季2台，最大旱季3台）Quantity:6 sets (all in operation in rain season,aver.2 and max.3in dry season)流量： Q=1910 L/sFlow quantity: Q=1910 L/s提上升度：H=8.28m（设计水位13.30m,提升后水位21.58m）Head: H=8.28m(min.water level 13.30,and 21.58 after pumpin

37、g)螺旋直径：D=2.850mDiameter of the screw:D=2.850m配套电机Engines设备数量：4套Quantity: 4 sets单台功率 N=250 kwPower for each: N=250 kw沼气发动机Biogas engines设备数量：2套Quantity: 2 sets单台功率 N=250 kwPower for each: N=250 kw所需沼气量 6178N m3/dBiogas needed: 6178N m3/d可利用余热 1237x104Kcal/dUsable remain heat: 1237x104Kcal/d -热回收系统 30

38、0KW -Heat recovery system 300KW -紧急冷却系统 96Kcal/s -Emergency air cooler 96Kcal/s -油泵 40l/h -Oil pump 40l/h叠梁闸门Pensrock数量：6套Quantity:6 sets(2) 细格栅站Fine screen station设计参数及描述Description of the design parameters细格栅站土建及设备规模均按一期规模设计并充分考虑与二、三期规模的连接。Scale of civil Engineering and equipments are set forth ac

39、cording to the first stage and give full consideration to the further second and third stage.设计流量：雨季最大流量Qmax=11.46 m3/sDesign flow quantity:Rain season Qmax=11.46 m3/s 旱季最大流量Q旱max=4.40 m3/s Dry season Q max=4.40 m3/s旱季平均流量Q平均=3.82 m3/sDry season Q aver. =3.82 m3/s设置细格栅可去除原水中漂移物以及杂物，保证后续处理流程的通畅，设有八条渠

40、道。八条渠道格栅前后分别装有闸门以便检修。细格栅的栅渣由螺旋传送至栅渣压实后送往栅渣箱中，污水经过细格栅后进入曝气沉砂池。细格栅站与进水泵房联建，单渠宽2.0m。The fine screen station is designed to remove floaters in the raw sewage to ensure a smooth flow in the following treatment. 8 channels, each is equipped with penstorks for maintenance, are set. Screens are removed by s

41、crew conveyor and crushed by screens presser, and sent into dustin. Sewage flows into aeration grit chamber after fine screen. Fine screen station is built together with inlet pump station, and single channel width is 2.0m.主要设备及参数Main equipments and parameters机械旋转细格栅Mechanical rotation fine screen数量

42、： 8台Quantity: 8 sets格栅宽度：B=1.8mWidth: B=1.8m栅条间隙： b=15mmClearance between bars: b=15mm格栅倾角：=70oInclination : =70o栅前水深：1.6mWater depth : 1.6m单台功率 N=2.2 kwPower for each: N=2.2 kw螺旋输送机Screw conveyor数量： 1台Quantity: 1 set规格： 6m3/h L=23mSpecification: 6m3/h L=23m单台功率： N=3.7kwPower for each set: N=3.7kw栅渣

43、压实机Screen presser数量： 1台Quantity: 1 set规格： 6m3/hSpecification: 6m3/h单台功率： N=1.5kwPower for each set: N=1.5kwa. 手动渠道闸门Manual Channel Penstock数量： 16套Quantity: 16 sets规格： 2.0m x 1.8mSpecification: 2.0m x 1.8m(3) 曝气沉砂池Aeration Grit ChamberA.设计参数及描述Description of the design parameters曝气沉砂池土建及设备规模均按一期规模设计并

44、充分考虑与二、三期规模的连接。Scale of civil Engineering and equipments are set forth according to the first stage and give full consideration to the further second and third stage.设计流量：雨季最大流量Qmax=11.46 m3/sDesign flow quantity:Rain season Qmax=11.46 m3/s 旱季最大流量Q旱max=4.40 m3/s Dry season Q max=4.40 m3/s旱季平均流量Q平均=3

45、.82 m3/sDry season Q aver. =3.82 m3/s沉砂池采纳曝气沉砂池系统，可去除原水中粒径较大的无机砂粒，以保证后续流程的正常运行。The aeration grit setting system of the grit chamber can remove the relative big inorganic granules to ensure a smooth flow in the following treatment.吸砂泵提升沉砂至砂水分别器，进行砂水分别。污水经沉砂池后进入氧化沟。罗茨鼓风机放置于进水泵房一层内。Grit removal pump ra

46、ises grits to grit classifier,which separate grit from water.The sewage flows into oxidation ditch after setting.The blowers are put in first floot of the pump station.采纳两组沉砂池系统（每组两池）。Two groups of grit chambers are adopted(each with two chambers).池数：4池Number of tanks:4 chambers雨季停留时间：2 minRetention

47、 time in dry seasons:5 min池长：L=30mLength of the chamber:L=30m池宽：B=4.0mWidth of the chamber:B=4.0m有效水深约 H效=3.0 mEffective water depth : Heffective=3.0 m所需空气量：1788 m3/hAir needed: 1788 m3/hB. 主要设备及参数Main equipments and parametersa. 刮砂桥Grit scraper数量： 2套（两池共用1套）Quantity: 2 sets(one for each two chamber

48、s)桥长： L=10mLength: L=10m单台功率： N=0.75kwPower for each set: N=0.75kwb. 吸砂泵Grit removeal pump数量： 4套Quantity: 4 sets规格： Q=40m3/h H=5mSpecification: Q=40m3/h H=5m单台功率： N=2.2kwPower for each set: N=2.2kwc. 罗茨鼓风机Blowers数量： 3套（二用一备）Quantity: 3 sets(one standby)规格： Q=895m3/h H=3.5mSpecification: Q=895m3/h H=

49、3.5m单台功率： 18kwPower for each set: 18kwd. 砂水分别器数量： 2套Quantity: 2 sets规格： Q=70120m3/hSpecification: Q=70120m3/h单台功率： N=1.1kwPower for each set: N=1.1kwe. 手动渠道闸门Manual channel penstock数量： 4套Quantity: 4 sets规格： 1.5m x 1.5mSpecification: 1.5m x 1.5mf. 手动渠道闸门Manual channel penstock数量： 4套Quantity: 4 sets规格

50、： 1.5m x 1.8mSpecification: 1.5m x 1.8m(4) 雨水溢流渠Rain Overflow ChannelA.设计参数及描述Description of the design parameters为矩形钢筋砼结构，池内设有调整堰板，雨季时可调整溢流量以保证进入氧化沟流量的稳定。在进入氧化沟渠道的入口处装有叠梁闸，雨季时可插入叠梁闸板以保证进入氧化沟流量的稳定。溢流后的雨水干脆排入低排沟，该渠道按一期规模设计。Rectangular reinforced concrete structure with adjustable weir in for adjustme

51、nt of overflow quantity in rain seasons to ensure stability in the oxidation ditches. Stop logs are installed in the entrance of the oxidation ditches, to ensure the stable operation of the oxidation ditches in rain seasons. The overflowed rain flows into Dipai Trough directly, and the overflow chan

52、nel is designed as the first stage (330,000m3/d).主要设计参数：Main design parameters:最大雨水溢流量 6.49m3/sMax.overflow quantity of the rain water: 6.49m3/s池长：20mLength of the tank:20mB. 主要设备及参数Main equipments and parametersa. 电动调整堰板Electric adjustable weir规格：L=5m H=0.5mSpecifications: L=5m H=0.5m单台功率： 0.75kwPo

53、wer for each set: 0.75kwb. 叠梁闸Stop logs规格：L= 2.5m H=0.4mSpecifications: L= 2.5m H=0.4m(5) 氧化沟Oxidation DitchesA.设计参数及描述Description of the design parameters池中设立式表曝机，获得动能和溶解氧的混合液在池中快速流淌，可形成好氧、缺氧区，具有降解有机物和脱氮的功能。为钢筋砼池。池内预留出安装水下推动器的位置，可依据以后实际运行状况确定。每座氧化沟通过渠道分别经计量后进水，可通过调整安装在进口处的调整堰确定进入每座氧化沟的流量，进水调整堰亦可起关闭

54、进水的作用。氧化沟出水处亦安装有调整堰以调整池内水位并可关闭出水。每池设有放空阀门。Rectangular reinforced concrete structure with adjustable weir in for adjustment of overflow quantity in rain seasons to ensure stability in the oxidation ditches. Stop logs are installed in the entrance of the oxidation ditches, to ensure the stable operati

55、on of the oxidation ditches in rain seasons. The overflowed rain flows into Dipai Trough directly, and the overflow channel is designed as the first stage (330,000m3/d).主要设计参数Main design parameters设计流量 旱季平均流量Q平均=3.82 m3/sFlow quantity: Average in Dry seasons: Q aver. =3.82 m3/s泥龄： 4天Sludge life: 4da

56、ys设计水温 18摄氏度Temperature of the sewage: 18degrees污泥负荷 0.204kgBOD5/kgMLSS日Sludge loading: 0.204kgBOD5/kgMLSSday污泥回流比 100%Sludge return rate: 100%污泥产率 1.35kgDS/kg BOD5Sludge production rate: 1.35kgDS/kg BOD5混合液浓度： 3.03.5g/LStrength of mixed liquid: 3.03.5g/L水深 5.0mWater depth: 5.0m池数： 8池Quantity of tan

57、ks:8 tanks曝气方式 立式表曝机Way of aeration: vertical surface aerator氧化沟总容积 8 x 9000 m3Total volume of the oxidation ditches: 8 x 9000 m3水力停留时间 5.1hHydraulic retention time: 5.1h实际平均需氧量为 35154kgO2/dActual average oxygen demand: 35154kgO2/d实际最大需氧量为 45700kgO2/dActual maximun oxygen demand: 45700kgO2/d标准状况下平均需氧量为(SOR) 59410kgO2/dAverage oxygen demand at standard conditions(SOR) 59410kgO2/d标准状况下最大需氧量为(SOR) 59410kgO2/dMaximun oxygen demand at standard conditions(SOR)59410kgO2/dB. 主要设备及参数Main equipments and para