《埃及海水淡化工程方案设计.doc》由会员分享，可在线阅读，更多相关《埃及海水淡化工程方案设计.doc（40页珍藏版）》请在三一办公上搜索。
1、Proposal of the Seawater desalination 埃及海水淡化工程方案设计1. Project Name工程名称NEW TECHNOLOGY CO-GENERATION POWER DESALTION PLANT(CPDP)中东欧电力和水项目公司新技术电力和海水淡化水共生厂2. Project Location 工程地点3. Available Site Area：可用占地面积12.5ha（250mx500m）for first phase, 25ha for the second phase.4. Project contents and scale 工程内容和规模
2、4.1 Product water for the first phase（2011） is 360000m3/d and 600000m3/d （2015） for the second phase. 36万m3/d海水淡化（2011）；60万m3/d（2015）4.2 The scale for bottled water is 3000m3/d 3000m3/d瓶装饮用水4.3 crystallized salt product 配套结晶盐项目According to the client requirement, this part is included in another pro
3、ject, so this cost is not in the offer of this project.根据业主要求，此部分另外立项考虑，投资不在本次报价范围内5. The raw seawater quality 进水水质情况 5.1 Water Quality at the Project Location Physico-chemical Analysis of Water Samples at the Project Location (Samples Delivery Date: 29 June 2008) 项目地点处水质情况如下（采用点时间为2008年6月29日）Parame
4、ters参数UnitConcentrationSite 1Site 2Site 3Site 4Site 5pH -8.07.98.08.07.8Water Temperature水温 oC2324.5252426Electrical Conductivity 电导率mho/cm6115059800620005920060500Transparency透明度 cm9090909090Total Dissolved Solids mg/I3950339557387953888939084Suspended Solids mg/I8.69.510.6108.9Total Solids mg/I395
5、11.639566.538791.63889939092.9Total Alkalinity (as CaCO3) mg/I120122124128116Chloride(CI-) mg/I2500025000250002500024000Sulfate (SO4 2-) mg/I421412439432438Nitrate (NO3-N) mg/I0.020.010.010.010.01Sodium (Na+) mg/I1150210842109121098710223Potassium (K+) mg/I753731692684613Manganese g/lNil0.020.270.65
6、0.11Calcium (Ca2+) mg/I561641561561601Magnesium (Mg2+) mg/I17031654160516541581Notes: (1) 100 m up stream. 水质采用点上游100米处，(2) 200 m up stream. 水质采用点上游200米处(3) fronting the power plant site. 水质采用点厂址前，(4) 100 m down stream. 水质采用点下游100米处，(5) 200 m down stream. 水质采用点下游100米处5.2 Surface Water Quality at 300
7、, 500 and 700 m in Three Profiles Extending Seaward form the Project Site (Hydraulics Research Institute, EDF Suez Gulf Power S.A.E., 2000)项目地点向海延伸300m，500m，700m处的表面水质情况：ParameterRangeAverageTemperature, oC17-18 17.3Salinity, % 盐分42.17-42.69 42.36DO, mg/l4.88-7.57 7.06DOM, mgO2/I0.36-2.02 1.47pH8.90
8、-8.2 8.12TSM, mg/l16-30.7 18.9Chl a, mg/l0.11-0.230.20NH4, mole0.1-2.4 0.75NO2, mole0.026-0.78 0.24NO3, mole0.003-0.248 0.128TN, mole1.58-11.66 6.20PO4, mole0.055-0.11 0.069TP, mole0.26-0.77 0.48SiO4, mole1.81-2.38 2.005.3 Water Quality at the Project Location Organic Analysis of Water Samples at th
9、e Project Location (1) (Samples Delivery Date: 29 June 2008)五处采样点水质的有机物分析情况ParametersUnitConcentrationSite 1Site 2Site 3Site 4Site 5CODmgO2/I3228322830BODmgO2/I16.216.5187.824.9Oil& Greasemg/I14.815.115.316.516.0Phenol 石碳酸mg/IN/D(2)N/DN/DN/DN/DPolycyclic Aromatic Hydrocarbons多环芳烃化合物mg/I 0.0410.0390.
10、0370.0380.0375Total Hydrocarbons总氢碳化合物mg/I 78.679.281.685.784.3Chlorinated Hydrocarbons 氯化烃mg/I 0.0340.0490.0530.0470.062Polychlorinated Biphenyles (PCBs) 多氯联苯mg/I 0.670.870.850.760.68Notes: (1) The same sampling points as indicated in Notes of （1）(2) ND = Not Detected.5.4 Heavy Metals Analysis of W
11、ater Samples (1)(Samples Delivery Date: 29 June 2008) 水样的重金属分析ParametersUnitConcentrationDetection Limits (2)Site 1Site 2Site 3Site 4Site 5Zinc 锌mg/IN/D(3)N/DN/DN/DN/D0.005Cadmium 镉mg/I0.1620.1580.1510.1420.140.002Chromium 铬mg/I0.0960.0890.0910.0920.0930.02Lead 铅mg/I1.0631.0341.0481.0521.0510.05Nick
12、el 镍mg/I0.6760.6690.6680.6720.6740.02Notes: (1) The same sampling points as indicated in Notes of Table（1） (2) Detection Limits: The sensitivity of the equipment. (3) ND = Not Detected.5.5 Microbiological Analysis of Water Samples(1) (Samples Delivery Date: 29 June 2008) 水样的微生物分析Site No.Total Bacter
13、ial Counts, Cell/cm3Most Probable Number Index / 100mIAt 22 oCAt 37 oCTotal Coliform总大肠杆菌Faecal Coliform粪大肠杆菌Site 164721.1 x 10270Site 251541.4 x 10270Site 359647030Site 442N/D (2)N/DSite 532N/DN/DNotes: (1) The same sampling points as indicated in Notes of Table (1). (2) N/D = Not Detected5.6 Algal
14、 Counts of Water Samples (*) (Samples Delivery Date: 29 June 2008) 水样的含藻类统计ParametersCount (Organisms/ml)Site 1Site 2Site 3Site 4Site 5Diatoms 硅藻类120 100 90 110 110 Green Algae 绿藻类10 10 10 10 10 Blue-Green Algae蓝藻类20 20 10 10 10 Total Algal Counts总藻类150 130 110 140 140 Notes: (*) The same sampling p
15、oints as indicated in Notes of （1）.5.6 Water Quality Assessment And Our Advice 海水水质评价和建议According to the seawater quality measurement and data (if right, verified), the seawater of this area contains oil, organics, heavy metal ion, and these materials contents have a high percentage. If intake such
16、seawater, it will increase the investment, cost and maintains of the seawater desalination plant, and as the same as the electric power plant. Therefore, our advices as follows:1. Please verify the position of the sampling points, detect measurements and data record. We will also coordinate with you
17、r part to this work after sign the agreement.2. If the data is exactly correct, the advice of altering the sample points or project site is much better. 根据上述海水水质检测数据（如果合适、无误），该处海水中油、有机物、重金属含量过高，如果取用这样的海水，不仅会增加海水淡化厂的投资、成本以及日常维护量，对电厂部分也是同样的。因此，我方建议：1. 请核实取水点位置、检测方法、数据记录等。协议签署后我方也会配合进行该工作。2. 如果数据无误，建议本
18、工程最好更换取水点或厂址。6. The requirement of product quality产品质量要求6.1 Desalination seawater product: with the following specifications脱盐海水产品的水质要求如下：ANIONSPPMCATIONSPPMBicarbonate重碳酸盐27Sodium钠离子10 -12Sulphate硫酸盐50Calcium钙离子3 - 4Chloride氯化物47Magnesium镁离子19Nitrate硝酸盐0 - 4Potassium钾离子0.1 - 0.2TDS (mg/l)130T. Hard
19、ness 硬度50pH7.8 8.06.2 Bottled drinking water with 250 ml, 500 ml, 1500 ml, 1 gallon, 6 gallons PET packaging with the following specifications: 产品瓶装水的水质要求如下：ANIONSPPMCATIONSPPMBicarbonate重碳酸盐50Sodium钠离子12Sulphate硫酸盐50Calcium钙离子15Chloride氯化物15Magnesium镁离子5Fluoride氟化物0.8Potassium钾离子0.2Nitrate硝酸盐0.1Iro
20、n铁离子0.02TDS (mg/l)110T. Hardness硬度50pH7.07. Introduction of the Process 工艺介绍The methods of seawater desalination are thermo method and membrane method as mechanism. Nowadays, the project of seawater desalination mainly has three techniques: MSF, MED and MVC. Membrane methods is referring to the SWRO
21、 techniques, which utilize semi permeable membrane, under a certain pressure it just allows the water permeate and then separate the impurity from the seawater. SWRO has become to the main techniques in the field of membrane techniques. thermo method is referring to the MED techniques, which is a ma
22、in technique in the field of thermo method. 海水淡化的方法按脱盐机理可分为热法和膜法，实用化的热法海水淡化工艺的主要有：多级闪蒸(MSF)、低温多效(MED) 和压汽蒸馏(MVC)三种技术。膜法主要指海水反渗透（SWRO）技术，它利用半透膜，在压力下允许水透过而使盐分和杂质截留的技术。其中低温多效（MED)已成为热法的主流技术，海水反渗透（SWRO）已成为膜法的主流技术。There are two problems in the process of thermo method of seawater desalination, one is the
23、 decay of the equipment, and the other is scaling on the heat-transfer pipe. To solve these two problems, widely used method is to use the corrosion-resistant alloy, and added the antisludging agent to the intake seawater. In addition, due to the corrosion and scaling velocity of the seawater and br
24、ine is related to the evaporation temperature, so in the field of seawater desalination to decrease the evaporation temperature of the seawater is a most important problem. This is why MED technique is rising in past dozens of years. A MED technique is generally operated in 70 centi degree, in this
25、temperature, when enrichment factor of seawater is 1.82.0, denuded zone of the calcium sulphate and carbonate is still removed from operating point, so the scaling probability is minimum. also because of the use of aluminium alloy, epoxy coating, plastic, which is corrosion-resistant in this tempera
26、ture, so MED equipment can be added only minimum antisludging agent to the seawater, not like MSF, which should be added acid to remove the CO2 and O2. So it can reduce the cost of investment and maintains. Therefore, in past few years, MED technique develops fast, and until 2001, MED separate unit
27、can reach a water yield of 68000m3/d. Also, the total volume of process water is exceeding to the MSF technique, and there are many operation outstanding achievements in the worldwide, and the technique has maturely used in the world.热法海水淡化工艺面临的两大问题是设备的腐蚀和海水在传热管上的结垢。为了克服这两个难题，广泛采用的办法是使用贵重的耐蚀合金、在进料水中
28、加入阻垢分散剂。另外，由于海水和浓盐水的腐蚀和结垢速度与其蒸发温度密切相关，在海水淡化领域也把降低海水的蒸发温度作为解决问题的突破口，这就是近十几年来兴起的低温淡化（MED)技术。低温多效蒸馏（MED)一般在70 以下进行操作，在这个温度下，海水的浓缩倍数为1.82时，硫酸钙和碳酸盐的结晶析出区还远离操作点，所以结垢倾向极小。又因铝合金、环氧树脂涂层、塑料的使用在该温度下能耐氧的腐蚀，因此低温多效蒸馏装置对进入装置的海水只需加入微量阻垢剂，而不需像多级闪蒸装置那样加酸脱除CO2及O2，因而降低了投资和操作成本。因此，近几年低温淡化（MED)发展迅速，到2001年低温多效（MED)单台最大产水量
29、已达到68000m3/d，其年总制水量也已超过MSF工艺，并在世界各地已由多台运行业绩，技术是成熟的。The SWRO technique has many advantages, such as low project investment, short construction period, small scale of plant area, simply operation maintains, low energy, low cost of water yield. After use the measure of energy recycle device and improvi
30、ng the water recycle rate. the energy consumption is great reduced in one unit of water yield, the energy consumption of the desalination seawater is decreased from 4.05.5 kwh/m3 per ton now to the 2.54.5 kwh/m3 per ton. As the development in these years, SWRO technique is become much more maturely
31、used, the production capacity of complete plant become much more powerful, the scale of project is much bigger. Therefore, the SWRO technique is become one of the main techniques in the field of seawater desalination.海水反渗透淡化技术（SWRO）具有工程投资低、建造周期短、占地面积小、运行维护简便、能耗低、制水成本低等优势。尤其是采用了更高效的能量回收装置、提高水回收率等措施后，
32、大大降低单位产水的能耗，海水淡化吨水能耗将由目前的4.05.5kwh/m3下降到2.54.5 kwh/m3。经过近几年的发展，反渗透海水淡化工程技术越来越成熟，成套设备制造能力越来越强，应用规模越来越大，海水反渗透海水淡化技术已逐渐成为海水淡化的主流技术之一。According to the raw seawater data, product water data of the project and application of brine, we recommend thermo and membrane hybrid technique: NF-RO-MED/TVC. The proc
33、ess flow sheet and water balance referred to figue7.17.2. The advantages of the process are showed as follows: it can be sharing the seawater intake; can be fully used low grade steam from the electric plant; the product water can satisfy the vary requirement as the certain proportion, so the cost o
34、f seawater desalination is reduced as well as the quantity of brine discharge. Nowadays, the largest of seawater desalination in the world, which is used thermo-membrane hybrid technique, its scale can be reached 454000m3/d, MSF water yield is 284000m3/d, RO water yield is 170000 m3/d根据本工程进水、产品水以及浓水
35、的用途，推荐采用热膜杂化工艺NF-RO-MED/TVC（纳滤-反渗透-多级蒸馏），工艺流程和水量平衡简图详见图7.1图7.2。该工艺具有以下优点：可以共用海水取水口，能够充分利用电厂低品位蒸汽，淡化产品水可以按一定比例混合满足不同需求需求，降低海水淡化成本，减少浓水排放量等。目前，世界上最大的热膜联产海水淡化厂已达454000m3/d，其中，MSF产水284000m3/d万立方米，RO产水170000 m3/d。Fig 7.1 Process Flow sheet图7.1 工艺流程图Fig 7.2 Water Balance Flow Sheet图7.2水量平衡图The whole seawa
36、ter treatment flow is included several parts as follows:整个处理流程可以分为以下几个部分：7.1 Seawater Intake System 海水取水系统We propose the mode of water intake adopt the artesian nullah. In order to avoid the influence of debris and biological in seawater, bar screen of 50mm and rotating mesh strainer of 4 4mm are se
37、t in the nullah. The water pumping station needs to design with 800000 m3/d.建议采用自流明渠引水的取水方式，为避免海水中杂物及生物的影响，在明渠内设置的50mm间隙粗格栅，44mm旋转筛网滤网。取水泵站采用按照80万m3/d设计。The inlet of priming nullah is more than 0.5cm lower than the guaranteed low tide level of the project needed, and setup the washing cycle accordin
38、g to the actual water quality.引水渠入口低于工程所要求的保证率低潮位以下大于0.5，并根据取水水质实际情况设定清洗周期。Fig 7.3 Coarse Screen Fig 7.3 Intake water pump station Screen图7.3粗格栅示意图 图7.4进水泵站示意图7.2 Pretreatment System 预处理系统Pretreatment is of the utmost importance for the seawater desalination, especially for the RO membrane. The RO m
39、embrane is more sensitive to the colloid, organism, microorganism, siliceous compound and other pollution in seawater; blockage, scaling and degradation may be caused by the pollutants, ultimately lead to the decline of seawater desalination rate and water production. Therefore, the seawater reverse
40、 osmosis desalination system has a special strict requirement on the pretreatment; the pretreatment is an important guarantee for the successful operation of the system.预处理对于海水淡化工程至关重要，尤其是反渗透膜对进水更加敏感，容易被水中的胶体、有机物、微生物、硅等物质污染，造成反渗透膜的污堵、结垢和膜降解，最终导致系统除盐率和产水量的下降。因此，反渗透海水淡化系统对海水预处理有着特殊严格的要求，预处理是反渗透系统成功运行的
41、重要保证。For the specific circumstances of this project, coagulative precipitation and multi-medium filter are recommend as the pretreatment. The main function is to remove the suspended solids, colloid, organism, germ, algae, halobios in the raw water.针对该项目的具体情况，推荐采用混凝沉淀及多介质滤池作为预处理手段。主要作用是去除原水中含有的悬浮物、胶
42、体有机污染物质、细菌、藻类、海生物等。7.2.1 Unit of Coagulative Precipitation混凝沉淀单元Coagulation and flocculation sedimentation tank is a pretreatment facilities which take charge of reaction, oxidation, inclined plate clarification and automatic sludge discharge. The filtration rate up to 20m/ h 30m/ h, which enable to
43、 reduce the floor space greatly, also makes setting roof on the top of the structure possible, in order to avoid the breeding of algae. The medicine generally adopt inorganic iron salts, aluminum salts, oxidizer, disinfectants and coagulant aid. When water quality break, oxidizer and powder activate
44、d carbon can be dosed as an emergency measure.混凝沉淀池是集絮凝反应、氧化、斜板澄清、自动排泥于一体的预处理设备，滤速可达20m/h30m/h，占地面积大大减小，这也使得池体顶部设置顶棚成为可能，从而避免藻类滋生。药剂一般可投加无机铁盐、铝盐、氧化剂、消毒剂、助凝剂等。水质突变时可以投加氧化剂和粉末活性炭作为应急措施。Fig7.5 coagulative precipitation tank图7.5 混凝沉淀池示意图7.2.2 Multimedia filtration unit多介质过滤单元Multimedia filter can make u
45、se of one or several media to remove suspended impurities, microorganisms and colloids from water. The filter commonly used are quartz sand, anthracite coal and manganese grain, which can be used in turbidity removal, water softening, and pretreatment of purified water, etc. 多介质过滤器是利用一种或几种过滤介质，有效去除水
46、中的悬浮杂质、微生物和胶体物质，使水澄清的过程。常用的滤料有石英沙，无烟煤，锰砂等，主要用于水处理除浊，软化水，纯水的前级预处理等。过滤速度一般小于8m/h，一般每天自动反冲洗一次。The quality of effluent treated by pretreatment system is as follows: turbidity 1NTU, CODMn 3 ppm, and SDI5, which protects the following equipment run firmly.预处理系统出水水质可以达到：浊度1 NTU；CODMn 3 ppm， SDI5，从而更有效地保护后续设备的稳定运行。Fig.7.6 Multime
