مجموعة تكنولاب البهاء جروب تحاليل وتنقية ومعالجة المياه |
تنظيف وتطهير وغسيل واعادة تاهيل الخزانات
معمل تكنولاب البهاء جروب للتحاليل الكيميائية والطبية والتشخيص بالنظائر المشعة للمخدرات والهرمونات والسموم وتحاليل المياه
مجموعة
تكنولاب البهاء جروب
لتصميم محطات الصرف الصناعى والصحى
لمعالجة مياه الصرف الصناعى والصحى
مجموعة تكنولاب البهاء جروب
المكتب الاستشارى العلمى
دراسات علمية كيميائية
معالجة الغلايات وانظمة البخار المكثف
معالجة ابراج التبريد المفتوحة
معالجة الشيللرات
مجموعة تكنولاب البهاء جروب
اسنشاريين
كيميائيين/طبيين/بكترولوجيين
عقيد دكتور
بهاء بدر الدين محمود
رئيس مجلس الادارة
استشاريون متخصصون فى مجال تحاليل وتنقية ومعالجة المياه
متخصصون فى تصنيع وتصميم كيماويات
معالجة الصرف الصناعى والصحى
حسب كل مشكلة كل على حدة تصنيع وتحضير كيماويات معالجة المياه الصناعية
مؤتمرات/اجتماعات/محاضرات/فريق عمل متميز صور من وحدات معالجة المياه
technolab el-bahaa group TECHNOLAB EL-BAHAA GROUP
EGYPT
FOR
WATER
TREATMENT/PURIFICATION/ANALYSIS
CONSULTANTS
CHEMIST/PHYSICS/MICROBIOLIGIST
INDUSTRIAL WATER
WASTE WATER
DRINKING WATER
TANKS CLEANING
CHAIRMAN
COLONEL.DR
BAHAA BADR EL-DIN
0117156569
0129834104
0163793775
0174041455 تصميم وانشاء محطات صرف صناعى/waste water treatment plant design technolab el-bahaa group egypt We are a consultants in water treatment with our chemicals as:- Boiler water treatment chemicals Condensated steam treatment chemicals Oxygen scavenger treatment chemicals Ph-adjustment treatment chemicals Antiscale treatment chemicals Anticorrosion treatment chemicals Open cooling tower treatment chemicals Chillers treatment chemicals Waste water treatment chemicals Drinking water purification chemicals Swimming pool treatment chemicals Fuel oil improver(mazote/solar/benzene) technolab el-bahaa group
egypt
We are consultants in extraction ,analysis and trading the raw materials of mines as:-
Rock phosphate
32%-30%-28%-25%
Kaolin
Quartez-silica
Talcum
Feldspae(potash-sodumic)
Silica sand
Silica fume
Iron oxid ore
Manganese oxid
Cement(42.5%-32.5%)
Ferro manganese
Ferro manganese high carbon technolab el-bahaa group
web sites
e-mails
water treatment unit design
وكلاء لشركات تركية وصينية لتوريد وتركيب وصيانة الغلايات وملحقاتها
solo agent for turkish and chinese companies for boiler production/manufacture/maintance
وكلاء لشركات تركية وصينية واوروبية لتصنيع وتركيب وصيانة ابراج التبريد المفتوحة
تصميم وتوريد وتركيب الشيللرات
design/production/maintance
chillers ابراج التبريد المفتوحة مجموعة تكنولاب البهاء جروب
المكتب الاستشارى العلمى
قطاع توريد خطوط انتاج المصانع
نحن طريقك لاختيار افضل خطوط الانتاج لمصنعكم
سابقة خبرتنا فى اختيار خطوط الانتاج لعملاؤنا
1)خطوط انتاج العصائر الطبيعية والمحفوظة والمربات
2)خطوط انتاج الزيوت الطبيعية والمحفوظة
3)خطوط انتاج اللبن الطبيعى والمحفوظ والمبستر والمجفف والبودرة
4)خطوط تعليب وتغليف الفاكهة والخضروات
5)خطوط انتاج المواسير البلاستيك والبى فى سى والبولى ايثيلين
6)خطوط انتاج التراى كالسيوم فوسفات والحبر الاسود
7)خطوط انتاج الاسفلت بانواعه
محطات معالجة الصرف الصناعى والصحى بالطرق البيولوجية والكيميائية
9)محطات معالجة وتنقية مياه الشرب
10)محطات ازالة ملوحة البحار لاستخدامها فى الشرب والرى
11)الغلايات وخطوط انتاج البخار الساخن المكثف
12)الشيللرات وابراج التبريد المفتوحة وخطوط انتاج البخار البارد المكثف
للاستعلام
مجموعة تكنولاب البهاء جروب
0117156569
0129834104
0163793775
القاهرة-شارع صلاح سالم-عمارات العبور-عمارة 17 ب فلا تر رملية/كربونية/زلطيه/حديدية
وحدات سوفتنر لازالة عسر المياه
مواصفات مياه الشرب
Drinking water
acceptable
values
50 | colour | acceptable | Taste | nil | Odour | 6.5-9.2 | ph |
1 mg/dl | pb | 5 mg/dl | as | 50 mg/dl | cn | 10 mg/dl | cd | 0-100mg/dl | hg | 8 mg/dl | f | 45 mg/dl | N02 | 1 mg/dl | Fe | 5 mg/dl | Mn | 5.1 mg/dl | Cu | 200 mg/dl | Ca | 150 mg/dl | Mg | 600 mg/dl | Cl | 400 mg/dl | S04 | 200 mg/dl | Phenol | 15 mg/dl | zn |
الحدود المسموح به
ا لملوثات الصرف الصناعى
بعد المعالجة
Acceptable
values
treated wate water
7-9.5 | ph | 25-37 c | Temp | 40 mg/dl | Suspended solid | 35 mg/dl | bod | 3 mg/dl | Oil & grase | 0.1 mg/dl | hg | 0.02 mg/dl | cd | 0.1 mg/dl | cn | 0.5mg/dl | phenol | 1.5 ds/m | conductivity | 200 mg/dl | na | 120 mg/dl | ca | 56 mg/dl | mg | 30 mg/dl | k | 200 mg/dl | cl | 150 mg/dl | S02 | 0.75 mg/dl | Fe | 0.2 mg/dl | Zn | 0.5 mg/dl | Cu | 0.03 mg/dl | Ni | 0.09 mg/dl | Cr | 0.53 mg/dl | لb | 0.15 mg/dl | pb |
محطات تحلية مياه البحر بطريقة التقطير الومضى على مراحل MSF+3.jpg (image)محطات التقطير الومضى لتحلية مياه البحر2 some of types of tanks we services
انواع الخزانات التى يتم تنظيفها
ASME Specification Tanks Fuel Tanks Storage Tanks Custom Tanks Plastic Tanks Tank Cleaning Equipment Double Wall Tanks Septic Tanks Water Storage Tanks Fiberglass Reinforced Plastic Tanks Stainless Steel Tanks Custom / Septic
مراحل المعالجة الاولية والثانوية والمتقدمة للصرف الصناعى
صور مختلفة من وحدات وخزانات معالجة الصرف الصناعى التى تم تصميمها وتركيبها من قبل المجموعة
صور من خزانات الترسيب الكيميائى والفيزيائى لوحدات معالجة الصرف الصناعى المصممة من قبل المحموعة
technolab el-bahaa group
technolab el-bahaa group technolab el-bahaa group technolab el-bahaa group technolab el-bahaa group technolab el-bahaa group technolab el-bahaa group technolab el-bahaa group technolab el-bahaa group technolab el-bahaa group مياه رادياتير اخضر اللون بريستول تو ايه انتاج شركة بريستول تو ايه - دمياط الجديدة مجموعة تكنولاب البهاء جروب
اسطمبات عبوات منتجات شركة بريستول تو ايه-دمياط الجديدة مياه رادياتير خضراء فوسفورية من انتاج شركة بريستول تو ايه بترخيص من مجموعة تكنولاب البهاء جروب
زيت فرامل وباكم DOT3
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| كيف تحسب سعة واحجام وقدرة معدات محطة صرف صناعى/Calculations Used in the Daily Operation of a Wastewater Treatment Facility | |
| | كاتب الموضوع | رسالة |
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Admin Admin
عدد المساهمات : 3762 تاريخ التسجيل : 15/09/2009 العمر : 57 الموقع : مصر
| موضوع: كيف تحسب سعة واحجام وقدرة معدات محطة صرف صناعى/Calculations Used in the Daily Operation of a Wastewater Treatment Facility الجمعة مارس 23, 2012 11:56 am | |
| Calculations Used in the Daily Operation of a Wastewater Treatment Facility
Several basic equations are used in calculations to determine things such as Weir Overflow Rate, Detention Time, SRT, etc. The formulas for area and volume appear below, along with examples
AREA
Area Formula Example
Rectangle (Length) x (Width) (35' L) x (12' W) = 420 sq. ft . Circle (0.785) x (Dia. sq.) (0.785) x (55') x (55') = 2,375 sq. ft
VOLUME
Volume Formula Example
Rectangle L x W x H 80'L x 25'W x 10"H = 20,000 cu. ft
Cylinder (0.785) x (Dia. sq.) x (H) (0.785) x (55') x (55') x (25') = 59,366 cu. ft
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| | | Admin Admin
عدد المساهمات : 3762 تاريخ التسجيل : 15/09/2009 العمر : 57 الموقع : مصر
| موضوع: رد: كيف تحسب سعة واحجام وقدرة معدات محطة صرف صناعى/Calculations Used in the Daily Operation of a Wastewater Treatment Facility الجمعة مارس 23, 2012 11:59 am | |
| Raw Influent Calculations Plant Influent Loadings
Determines the influent loadings of pounds (BOD, TSS, etc.) to a wastewater treatment facility.
Plant Influent Loadings:
mg/l x mgd x 8.34 = lbs./day
Example (using TSS
Plant Conditions
TSS Influent = 135 mg/l
Influent flow = 1.5 mgd
To determine pounds into the plant, use the following calculation
mg/l x mgd x 8.34 = lbs/day
Example: 135 mg/l x 1.5 mgd x 8.34 = 1,688.85 lbs
This reflects the pounds of TSS into the plant on that particular day
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| | | Admin Admin
عدد المساهمات : 3762 تاريخ التسجيل : 15/09/2009 العمر : 57 الموقع : مصر
| موضوع: رد: كيف تحسب سعة واحجام وقدرة معدات محطة صرف صناعى/Calculations Used in the Daily Operation of a Wastewater Treatment Facility الجمعة مارس 23, 2012 12:05 pm | |
| Clarifier Capacity Calculations
Surface Loading Rate - RECTANGULAR Clarifier
Gallons of wastewater applied to each square foot of the clarifier area. This affects the settleable solids and BOD removal efficiency in the sedimentation process
Surface Loading Rate (RECTANGULAR CLARIFIER
gpd
sq. ft. of clarifier
Example
Clarifier
Length = 75 feet
Width = 12 feet
Influent flow = 1.2 mgd (1,200,000 gpd ) The square footage of the clarifier is L x W
75 x 12 = 900 sq. ft. To determine the Surface Loading Rate of a rectangular clarifier, use
the following calculation
gpd
sq. ft. of clarifier
Example: 1,200,000 gpd = 1,333 gpd/sq. ft
900 sq. ft. Clarifier Capacity Calculations
Surface Loading Rate - CIRCULAR Clarifier
Gallons of wastewater applied to each square foot of the clarifier area.
This affects the settleable solids and BOD removal efficiency in the se dimentation process
Surface Loading Rate (C IRCULAR CLARIFIER
gpd
sq. ft. of clarifier
Example
Clarifier
Diameter = 60 feet
Influent flow = 2,200,000 gpd
The square footage of the clarifier is .785 x Dia. sq
.785 x 60' x 60' = 2,826 sq. ft. To determine the Surface Loading Rate of a circular clarifier, use the
following calculation
gpd
sq. ft. of clarifier
Example: 2,200,000 gpd = 778.48 gpd/sq. ft
2,826 sq. ft. 3
Clarifier Capacity Calculations
Detention Time
Period of time that a particle remains in a tank
Detention Time
tank volume x 24 hours
Influent flow
Example (rectangular clarifier
Clarifier
Length = 75 feet
Width = 30 feet
Depth = 10 feet
Influent flow = 2,850,000 gpd
The volume of the clarifier is L x W x H x 7.48
70 ' x 25' x 10' x 7.48 = 130,900 gals. To determine the Detention Time of a rectangular clarifier, use the
following calculation
tank volume x 24 hours
Influent flow
Example: 130,900 gals x 24 = 1.10 hours
2,850,000
Weir Overflow Rate
gpd flow
Total feet of weir
Example
Plant Conditions
Weir length = 100 feet
Flow rate = 1,500,000 gpd
To determine the Weir Overflow Rate, use the following calculation
gpd flow
Total feet of weir
Example: 1,500,000 gpd = 15,000 gpd/ft
100 feet of weir
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| | | Admin Admin
عدد المساهمات : 3762 تاريخ التسجيل : 15/09/2009 العمر : 57 الموقع : مصر
| موضوع: رد: كيف تحسب سعة واحجام وقدرة معدات محطة صرف صناعى/Calculations Used in the Daily Operation of a Wastewater Treatment Facility الجمعة مارس 23, 2012 12:10 pm | |
| Activated Sludge Calculations Sludge Age Average time a particle of suspended solids remains in the activated sludge system. Sludge age is used to maintain the proper amount of activated sludge in the aeration system. To determine sludge age, you must calculate both the daily amount of suspended solids and the total amount of solids in the aerator. Sludge Age: Total lbs. of MLSS in aerator Daily lbs. of MLSS in aerator Example: Suspended solids of primary effluent = 110 mg/l Influent flow = 2.5 mgd Aeration tank volume = .5 mg MLSS concentration = 2,200 mg/l The plant influent loading = mg/l x mgd x 8.34 Example: 110 x 2.5 x 8.34 = 2,293.5 lbs. daily of SS (lbs of MLSS in aerator) 2,200 x .5 x 8.34 = 9,174 lbs. total of MLSS in aerator With these calculations, you can determine Slude Age: Total lbs. of MLSS in aerator = Days Sludge Age Daily lbs. of MLSS in aerator Example: 9,174 lbs. total of MLSS in aerator = 4 Days Sludge Age 2,293.5 lbs. daily of MLSS in aerator Example: Influent suspended solids = 250 mg/l Influent flow = 2.5 mgd Aeration tank volume = .5 mg MLSS concentration = 2,200 mg/l The plant influent loading = mg/l x mgd x 8.34 Example: 250 x 2.5 x 8.34 = 5,213 lbs. daily of SS (lbs of MLSS in aerator) 2,200 x .5 x 8.34 = 9,174 lbs. total of MLSS in aerator With these calculations, you can determine Slude Age: Total lbs. of MLSS in aerator = Days Sludge Age Daily lbs. of MLSS in aerator Example: 9,174 lbs. total of MLSS in aerator = 1.76 Days Sludge Age 5,213 lbs. daily of MLSS in aerator 5 Sludge Age - Plants with Primary Clarifier Sludge Age - Plants without Primary Clarifier Using these figures, calculate the amount of suspended solids leaving the system: Example: (7,250 mg/l waste sludge) x (.08 waste sludge flow) x (8.34 lbs.) + (20 mg/l SS final effluent) x (4.3 MGD influent flow) x (8.34 lbs.) = 4,837.2 lbs. SS + 717.2 lbs. SS = 5,554.4 lbs. SS leaving system For this example, the volume of the aeration tank and clarifier equals 1.7 mg. Pounds of Aeration Tank MLSS = Aeration Tank mg/l MLSS x mg x 8.34 Example: 2,500 mg/l MLSS x 1.7 mg volume x 8.34 lbs. = 35,445 lbs. MLSS Solids Retention Time (SRT): SRT days = lbs./day of SS in system lbs./day of SS leaving system Example: 35,445 lbs. MLSS = 6.38 SRT 5,554.4 lbs. SS leaving system Activated Sludge Calculations Solids Retention Time (SRT) Average time a given unit of cell mass stays in the activated sludge system. SRT is based on solids leaving the Activated Sludge process, and includes solids in the clarifiers. Also called MCRT (Mean Cell Residence Time). Solids Retention Time (SRT): SRT days = lbs./day of SS in system lbs./day of SS leaving system Factors in determining SRT: 1. Solids leaving the system (wasted) 2. Solids leaving the system (SS in the final effluent) 3. Solids in the system (aeration basins and clarifiers) Example: Tank volumes: Aeration volume = 1.6 mg Final Clarifer volume = .10 mg SS Concentration: Final effluent = 20 mg/l Waste sludge SS = 7,250 mg/l Aeration Tank MLSS = 2,500 mg/l Flows: Influent flow = 4.3 mgd Waste sludge flow = 0.08 mgd (24-hour period) 6 Solids to be Wasted Solids (measured in pounds) to be wasted over a set period of time (typically daily). Solids to be Wasted: Current inventory - Desired inventory to achieve peak performance = Pounds to be wasted After calculating the MLSS Concentration (see above), use the following formula to determine the pounds of solids to be wasted. Example: Peak performance = 22,000 pounds of MLSS in aeration system Current inventory = 25,000 pounds of MLSS in aeration system 25,000 pounds (current inventory) - 22,000 pounds (desired inventory) = 3,000 pounds to be wasted 7 MLSS Concentration in Pounds Pounds of MLSS in the aeration system. MLSS Concentration: MLSS (mg/l) x volume of aeration tank x 8.34 Example: MLSS in aeration tank = 2,500 mg/l Aeration system volume = 1.4 mg MLSS (mg/l) x volume of aeration tank x 8.34 2,500 mg/l x 1.4 x 8.34 = 29,190 lbs. of MLSS Activated Sludge Calculations F/M Ratio Ratio of food (biochemical oxygen demand) entering the aeration tank to microorganisms in the tank. F/M Ratio: lbs./BOD lbs. MLSS Example: lbs. of BOD entering plant daily = 4,340 lbs. lbs. of MLSS in aerator = 8,201 lbs. lbs. BOD or 4,340 lbs. of BOD entering plant daily = .53 F/M lbs. MLSS 8,201 lbs. of MLSS in aerator Activated Sludge Calculations Waste Sludge Pumping Rate Rate at which to pump the sludge to be wasted from the system. Normally expressed in gallons per minute (gpm). Example: Plant Conditions: lbs. of MLSS to be wasted = 1,400 lbs. MLSS concentration = 5,900 mg/l lbs. to be wasted = flow rate (mgd) MLSS concentration x 8.34 Example: 1,400 lbs. to be wasted = .0284 mgd wasting rate 5,900 mg/l x 8.34 Convert million gallons per day to gallons per day: mgd wasting rate x 1,000,000 = gpd wasting rate Example: .0284 x 1,000,000 = 28,400 gpd Convert gallons per day to gallons per minute (over 8 hours): gpd wasting rate 480 minutes (8 hours) Example: 28,400 gpd = 59.166 gpm 480 minutes | |
| | | Admin Admin
عدد المساهمات : 3762 تاريخ التسجيل : 15/09/2009 العمر : 57 الموقع : مصر
| موضوع: رد: كيف تحسب سعة واحجام وقدرة معدات محطة صرف صناعى/Calculations Used in the Daily Operation of a Wastewater Treatment Facility الجمعة مارس 23, 2012 12:14 pm | |
| Typical WWTP Operational Parameters [img] [/img] | |
| | | Admin Admin
عدد المساهمات : 3762 تاريخ التسجيل : 15/09/2009 العمر : 57 الموقع : مصر
| موضوع: رد: كيف تحسب سعة واحجام وقدرة معدات محطة صرف صناعى/Calculations Used in the Daily Operation of a Wastewater Treatment Facility الجمعة مارس 23, 2012 12:16 pm | |
| Metal Salt Addition for Phosphorus Removal Using metal salt chemical data, theoretically calculate the amount of chemical salt solution to add in gallons per day to remove phosphorus. * Values that need to be entered are shown in the gray boxes. Step 1. Determine the amount of influent phosphorus to remove. Influent flow in MGD Influent P (mg/l) lbs/gallon lbs of P to remove 2 x 8 x 8.34 = 133 Step 2. Determine the pounds of metal salt in a gallon of solution knowing the specific gravity. Specific gravity lbs/gal lbs metal salt/gal 1.4 x 8.34 = 11.7 Chemical Specific Gravity Alum 1.33 Ferric Chloride 1.441 Ferrous Chloride 1.23 Ferrous Sulfate 1.185 Step 3. Determine the pounds of actual metal in a gallon of metal salt solution with certain percentage metal content (provided by chemical supplier). lbs metal salt/gal % metal lbs metal/gal metal salt solution 11.7 x 12.5 = 1.5 Step 4. Look up removal ratio for the metal salt being used. Chemical Removal Ratio Alum 0.87 to1 Ferric Chloride 1.8 to 1 Ferrous Chloride 2.7 to 1 Ferrous Sulfate 2.7 to 1 Step 5. Determine the pounds of metal needed to remove the incoming pounds of phosphorus. Removal ratio Influent lbs of P lbs of metal to add 1.8 x 133 = 240 Step 6. Determine the gallons of metal salt solution with a certain percentage metal content to thus add. lbs of metal to add lbs of metal/gal gal/day of metal salt solution to add 240 ÷ 1.5 = 165 This estimate may be different than the value obtained from a calculator due to rounding differences. | |
| | | | كيف تحسب سعة واحجام وقدرة معدات محطة صرف صناعى/Calculations Used in the Daily Operation of a Wastewater Treatment Facility | |
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