Microsoft PowerPoint - DHP_MVR-Brief_New Model_EDU_130802_해양대_ver2.pptx

Size: px

Start display at page:

Download "Microsoft PowerPoint - DHP_MVR-Brief_New Model_EDU_130802_해양대_ver2.pptx"

정산 선
6 years ago
Views:

1 DHP 소개자료 Turbo MVR Distiller : Distiller System using Turbo Mechanical Vapor Recompression for Energy Recovery 증발법담수장비의기술진보와국내외현황 대원열판 1 P_1

Status of World Water Shortage Because of the increase of the world's population, especially

under rapid economic growth, significant reduction of water use per capita is happening.

generated by the rapid industrialization are contaminating the ground and the underground

2 Status of World Water Shortage Because of the increase of the world's population, especially countries like Indonesia, Vietnam, India, and etc. under rapid economic growth, significant reduction of water use per capita is happening. The deepening of uneven distribution of global water resources, is occurring significant water shortages in specified countries. (1/5 countries around the world, 3 billion people) Large amounts of sewage and waste water generated by the rapid industrialization are contaminating the ground and the underground water. The reduced amount of drinkable clean water causes various waterborn diseases. (each year, 5 million people killed) Now, we have to recognize the need for high efficient distiller equipment P_2

3 Water Conversion methods 가뭄 Drought Sea Water [ RO Filter Method ] Contaminated 폐수 Water Waste water disposal [ Evaporation Method ] P_3

4 RO Conversion Method Reverse Osmosis (RO) Filter System and Actual Operating Environment in Korea : - Need for clean sea water : Serious sea water contamination issue in the island regions in the west and south seas ->Demand for tube well - Must Operate Continuously : Intermittent operation, frequent filter replacements, unexpected increase of cost. - Bacillus Not Eliminated : Dosing of chemicals (condenser, reducer: sulfuric acid, chlorine), increase of operating cost - Pre and Post Treatment Systems / Professional Operator Required : Accident and risk in the handling of dangerous chemicals by non-professionals, operating cost increase P_4

Evaporation Conversion Methods Evaporation(MED, MSF, MVR)

water and any source water -> Appropriate for west

No special need for pre and post treatment systems/dosing

-> Reduced operating cost - No need for sterilization

package/automation -> Long life, possible to move to an

5 Evaporation Conversion Methods Evaporation(MED, MSF, MVR) Distiller System : - Irrelevant to the cleanness of sea water and any source water -> Appropriate for west sea/south sea, flood swept area(muddy water) in Korea - No special need for pre and post treatment systems/dosing of chemicals/parts which need to be replaced periodically -> Reduced operating cost - No need for sterilization (chlorine) -> 100% automatic high-temperature sterilization (Absolutely no virus!!!) - Non-corrosive material/transportable small package/automation -> Long life, possible to move to an arbitrary location Vacuum pump Steam Steam Cooling water Raw Water Pure Water Multi Effects Distiller (MED) P_5

6 MVR 법과 RO 법담수장비의특징비교 Evaluation Items MVR Distiller RO Distiller ETC 평가항목해설 Contamination of inflow seawater Not Effected Critical Issue Needs Tube Well, Pretreatment Facility Chemical dosing No Needed Absolutely Needed sulfuric acid, chlorine, Fecl3 etc 유입원수의수질의청정도 화학약품의사용여부 Sterilizing for water No Needed Absolutely Needed 물제조후소독필요성 Pre_Treatment Facility No Needed Absolutely Needed 전처리설비유무 Post_Treatment Facility No Needed Absolutely Needed 후처리설비유무 Quality of Drinking Water Very good (TDS<100ppm) good (100<TDS<500ppm) TDS<500 (ppm) in Korea Standard of Drinking water 제조된물의질 Main A/S Items Seal part of Low Parts of High Pressure MVR : 1-2 2(kgf/cm2) 주요 A/S 발생부품 Pressure Commercial Pump RO : (kgf/cm2) Pump System Constituents Very Simple Very Complex 장비구성의간편정도 Brine Disposal No chemicals, No Environmental severity Needs of Special 농축해수의배출시문 Problems with various Chemicals pollution treatment 제 facility Periodic Replacing Items Not Filters (NF, RO) 주기적인교체부품유 무 Operation Cost per ton of water (US$) ( 한국수자원공사보고서 ) Case in Korea : 5.5 (cent/kwh) 먹는물 1 톤제조비용 Initial Cost of Distiller High Low 초기투자비 Usage of Brine Yes (Salt, Minerals) No (with various 농축해수의재사용가능 (Concentrated sea water) Chemicals) 여부 Technology Level High Low Possible in advanced Nations 기술적수준 P_6

7 Energy Recovery Mechanism of Evaporation System Our Goal : Energy Recovery => Energy Saving => Low Operation Cost! 20 kcal Cooling water Steam Steam Steam Compressor Raw Water 620 kcal 1 Stage Effect (SE) 1 Liter Pure Water Multi Stage Effects Distiller (MED) 1 Liter Pure Water Mechanical Vapor Recompression (MVR) Methods 1 Stage 2 Stage ~ 10 Stage MVR Input Energy (kwh/ton) ~ * Coefficient of Performance (COP) = 620 (kcal) / 20 (kcal) = 31 P_7

Energy Saving Mechanism of Turbo_MVR System

20 kcal Steam Compressor Auxiliary Heater 107

Circulation Pump 1 Liter Pure Water [ Graphical

80(Kcal) Heat Exchanger [ Detail View of MVR ]

Concentrate (concentrated water) Raw Water: 20

Sensible Heat * COP = 620 (kcal) / 20 (kcal) = 31

anger Retrieve Latent Heat Steam: 100 Steam: 107

8 Energy Saving Mechanism of Turbo_MVR System Evaporative Condenser Tank 100 Steam Motor Steam 20 kcal Steam Compressor Auxiliary Heater 107 Steam Turbo Steam Compressor [ Type 1] Circulation Pump 1 Liter Pure Water [ Graphical View of MVR ] [ Energy Balance Scheme of MVR ] 80(Kcal) Heat Exchanger [ Detail View of MVR ] 540(Kcal) Condensed Water Sea Water /Waste Water Concentrate (concentrated water) Raw Water: 20 Fresh Water: 25 He eat Excha anger Retrieve Sensible Heat * COP = 620 (kcal) / 20 (kcal) = 31 Raw Water: 100 Fresh Water: 107 He eat Excha anger Retrieve Latent Heat Steam: 100 Steam: (Kcal) Stea am Compr ressor Motor Driving Electric Energy = 23.3 (Watt.h/Liter) P_8

Turbo-MVR 장치의 ENERGY BALANCE 온도1 t 107 100 포화액체라인포화증기라인 회전수잠열열전달 6 5 2 3 4 * 4 1.3 atm 1 atm 에너지투입 1. 잠열열전달위해, 증기 1.3기압압축, 설계온도차 7( 도 ) 생성 2. 온도차는압축기회전수로조절가능 3.

9 Turbo-MVR 장치의 ENERGY BALANCE 온도1 t 포화액체라인포화증기라인 회전수잠열열전달 * atm 1 atm 에너지투입 1. 잠열열전달위해, 증기 1.3기압압축, 설계온도차 7( 도 ) 생성 2. 온도차는압축기회전수로조절가능 3. 투입에너지를줄이기위해, 압축기고효율화필수 현열열전달 4. 연속적증기발생위해열교환기최적설계 / 순환량선정필수 엔트로피 잠열 : 539 (kcal/kg) 현열 : 80 (kcal/kg) 3 투입에너지 : 20 (kcal/kg) = 보유에너지 : 639 (kcal/kg) P_9 5

10 Turbo_MVR 법장비의 Schematic Diagram : 10 P_10

11 Example of Installation : Turbo MVR Waste Water Conversion System Private Waste Water Treatment Companies : 75 ~100 (ton/day ) P_11

12 New MVR Distiller Model Sample Drawing : 20 feet Mobile Model 12 P_12

13 New MVR Distiller Model Sample Drawing : 40 feet Mobile Model 13 P_13

Main Business Item : Drinking Water Conversion System Turbo-MVR system converting sea /dirty/infected water into the pure di drinking water - Can be applied for any

100% sterilization with high temperature : Naturally getting ZERO Virus water!

14 Main Business Item : Drinking Water Conversion System Turbo-MVR system converting sea /dirty/infected water into the pure di drinking water - Can be applied for any water : sea water, saline water, contaminated & infected ground/underground water, muddy water - No level of cleanness of raw water - No need of pre & post treatment - 100% sterilization with high temperature : Naturally getting ZERO Virus water! - Available for small size/integrated and fixed type/transportable type : Can be installed in any location (20 feet standard container size) - No Need of Periodic Parts Replacement - No Chemicals Dosing - Automated Operation : No need of special operator P_14

15 Example of Installation : Turbo MVR Drinking Water Conversion System Busan New Port Control Center : 20 ~ 50 (ton/day ) Maritime Affairs and Fisheries Office Control Center Busan New Port Gadeokdo Geoje-do - System No. 1 installed on August 30, 2005 P_15

16 Drinking Water Quality Check By National Agency Raw water (colored sea water : 35,000 ppm) Distilled water ZERO Bacillus ZERO bacterium Residual/Input = 126/35,000 = 0.36 (%) 99.64(%) Eliminatedi P_16

17 성능평가 ( 한국에너지기술연구원 ) 기록 / 환산항목자체평가공인기관평가 누적시험시간 (Hr) 1, 평균원수온도 ( 도 ) 평균증기온도 ( 도 ) 평균담수유량 (Liter/hr) 1,000 1,007.8 평균압축기동력 (kw) 적산총담수량 (Liter) 1,444, 적산총전력량 (kwh) 43, 압축기근거 성적계수 (COP) MVR 시스템근거성적계수 (COP) 전력소모량 (Watt.h/Liter) 에너지절약율 (%) P_17

18 Applications : Turbo_MVR Drinking Water Conversion System [Dirty Water Source] [Turbo_MVR Distiller] [Pure Drinking Water] Energy Recovery Process [Capacity : 100 ton/day] - [1 Liter Bottle] [100,000 Bottles/Day] [YES] [Infected Muddy River & Underground Water Source] Public Water Treatment School & University Public Restaurant Infant If supply pipe damaged, Water infected [No] Swimming pool Factory Hospital P_18

Water Production Cost Analysis & Model Spec. of Turbo_MVR L H W [Turbo_MVR Distiller Model & Dimension ] Model Capacity Dimension (meter) Weight (m 3 /day) (ton/day) L W H (ton) ADR 50 50 6.0 2.5 2.

19 Water Production Cost Analysis & Model Spec. of Turbo_MVR L H W [Turbo_MVR Distiller Model & Dimension ] Model Capacity Dimension (meter) Weight (m 3 /day) (ton/day) L W H (ton) ADR ADR (ft) Standard High Cubic ADR Container Size 17 Delivery (months) On FOB Test before delivery 4 6 Witness test On factory Components Installation All in One on 1 bed frame [** ADR (Advanced Distiller ) : Brand Name of Turbo MVR system ] [100 ton/day] - [100,000 Bottles(1 Liter) / Day] [ Electric Energy Required for Water Production ] [ Estimated number of persons to drink ] = 40 (Watt.hour/Liter) = 40 (kwh/ton) (* for all components in Turbo MVR ) [ Water Production Cost ] = 40 (kwh/ton) * 60 (Won/kWh) = 2,400 (Won/ton) in case of KOREA (1KWh=60 Korean Won) = 2.4 (Won/Liter) 1) If 1 person needs 10 (liter/day) of water 100,000 (liter/day)/10 (liter/day) = 10,000 (persons) 2) If 1 person needs 100 (liter/day) of water 100,000 (liter/day)/100(liter/day) = 1,000 (persons) 3) If 1 person needs 200 (liter/day) of water 100,000 (liter/day)/200(liter/day) = 500 (persons) 4) If 1 person needs 300(liter/day) of water 100,000 (liter/day)/300(liter/day) = 330 (persons) P_19

Extra Model of Turbo_MVR Tiling-Up Model Model Capacity (m3/day) (ton/day) Dimension (meter) L W H Weight (ton) Delivery (months) On FOB Test before delivery Components Installation ADR 300 300 6 2.

20 Extra Model of Turbo_MVR Tiling-Up Model Model Capacity (m3/day) (ton/day) Dimension (meter) L W H Weight (ton) Delivery (months) On FOB Test before delivery Components Installation ADR * *3 ADR *5 2.5* *5 5-8 ADR 1,000 1, * *10 Witness te st at factory per set All in One on 1 bed frame. App. 20(ft) High Cubic Container Size [ Tiling-Up Model : ADR 500 ] [ ADR 100 ] [ ADR 100 ] [ ADR 100 ] [ ADR 100 ] [ ADR 100 ] Raw water supply (sea water/brackish water) Raw water supply pipe Condensed water pipe pp Concentrated water pipe Drinking Water Tank Rejected Water Tank P_20

21 Water Recovery Rate and Power Consumption Type TDS(ppm) Recovery Rate(%) Power consumption (kwh/ton) Remark Sea Water 15,000~50, ~ 85% 30.3 ~ 63.3 * TDS : Total Dissolved Solid Brackish Water 1,500~15, ~ 98% 27.0 ~ 30.3 Underground Water More than 90% It depends on the amount of TDS The input raw water can be concentrated until max. 100,000ppm(=10% density) by MVR Distiller Water recovery rate = {1-TDS/(100,000ppm)}* Example : in case of TDS 15,000 of input raw water Water recovery rate ={1-15,000/100,000}*100=85%, Rejected water rate : 15% It means we are able to extract pure drinking water of 85% from input raw water. Power consumption calculation formula, based on our experiences : Power consumption(kwh/ton) = 145/100 * (concentration)^ Example : in case of TDS 15,000 of input raw water, concentration may be 1.5, expressed by percentage of density of impurity dissolved in water. Power consumption = 145/100 * 1.5^ = 30.3(kWh/ton) 3(kWh/ton) P_21

22 Turbo Steam Compressor : P_22

23 Turbo Steam Compressor : Essential Items of Turbo_MVR P_23

24 Aerodynamic Analysis for Turbo Steam Compressor Q3D F3D P_24

25 3-Dim. Impeller Blade manufacturing using 5 axes CNC machines Simulation of Tool Path P_25

26 증발법담수장비의종류와 MVR 법장비의경쟁력비교 방식 MVR TVC MED MSF 비고 에너지상대효율 단기준 장비상대크기극소소중대대동일용량 소요에너지종류전기전기 + 증기전기 + 증기전기 + 증기 - 설비용량소중대대 기술수준최상상중하 전문업체명 Sasakura( 일본 ) 대원열판 ( 한국 ) IDE( 이스라엘 ) 구비조건 - Sasakura( 일본 ) 고압증기보일러구비필수 MVR 은기술선진국제품임 현대중공업두산중공업 - 발전소증기폐열입수필수 발전소증기폐열입수필수 P_26

27 국내외 MVR 장비의핵심부품인증기압축기의회전체특성검토 : A/S 난이도와연관 - 극대 : 직경 2,000 (mm) 이상 - 대 : 직경 1,500-2,000 (mm) - 소 : 직경 (mm) 대 소 극대 SASAKURA( 일본 ) DHP Engineering( 한국 ) IDE ( 이스라엘 ) Q=150(T/D), L6000,W6000,H5000 Q= (T/D), L6000,W2500,H2900 Q= (T/D), L9500,W4500,H6100 P_27

28 국내의악성폐수처리현황과방안 폐수처리의필요성 악성폐수의국지적, 산발적발생 혼합집중화처리에막대한국가예산투입 ( 폐수처리효율미비 ) 국지적발생악성폐수의처리투명성요구 ( 환경오염문제대두 ) 해양투기방지법발효 (2013년) 해결방안 하류공공처리부하감소 처리효율고도화위해고효율수처리장치개발필수 악성폐수의국지적현지처리도모, 물환경개선효과극대 28 P_28

고효율고속터보기계기술,,,, 폐수 터보 (Turbo) = 폐수 (Waste Water) 폐수를살아있는물로 증발법 MVR 폐수처리장치의설치운용상효과 : - 비휘발성폐수종류무관 -> 다용도 - 주기적인교체부분전무 > > 운용비절감 - 약품투여전무 > 운용비절감 - 소독불요 > 100% 살균 > 운용비절감 - 전후처리장치불요 -> 설치면적최소!

29 고효율고속터보기계기술,,,, 폐수 터보 (Turbo) = 폐수 (Waste Water) 폐수를살아있는물로 증발법 MVR 폐수처리장치의설치운용상효과 : - 비휘발성폐수종류무관 -> 다용도 - 주기적인교체부분전무 > > 운용비절감 - 약품투여전무 > 운용비절감 - 소독불요 > 100% 살균 > 운용비절감 - 전후처리장치불요 -> 설치면적최소!!!!!!!! - 운전요소 >( 생물화학량 ] 에서->[ 물리량 : 온도 / 압력 ] 으로!! - 설치장소불문 > 소수수요에대처가능 - 장치구성요소의소형화 -> 운반식팩키지화가능 증발법 MVR 폐수처리장치의폐수처리비용효과 : 폐수처리방법성적계수톤당처리비 ( 천원 ) 비고 단일효용방식 중효용방식 단일 TVR 방식 단일 MVR 방식 폐수처리위탁비용 : 톤당 ( 천원 ) 근거 : 한국에너지기술연구소자료 P_29

30 폐수처리유사제품과특성비교 성능구분국내유사경쟁제품국외유사경쟁제품 관련회사명주요용도증기압축방식증기압축기특성증기냉각처리설비보일러설비적용가능폐수성상에너지절약정도폐수처리단가소비증기특성소음경제적설치위치설치면적구동방식이동성주요근거자료 A_SH/B_HE/C_JE 악성폐수처리, 해수담수화, 농축기열증기압축법 (TVC) 이젝터, 소형, 단순절대필요, 대용량대용량필요악성폐수 (COD: 수만ppm) 열펌프성적계수 (COP) 2 25,000 ( 원 / 톤 ) 고압증기, 대량소비증기파찰소음심함증기단가낮은소각장, 발전소적음고압증기와전기없음 ( 고정형 ) 자체인쇄및인터넷홍보물근거 일본 S사악성폐수처리, 해수담수화, 농축기기계식증기재압축법 (MVR) 대형송풍기 (3,600rpm), 대형, 정밀기계불요불요악성폐수 (COD: 수만ppm) 열펌프성적계수 (COP) 13 3,000 ( 원 / 톤 ) 불요보통임의장소아주적음전기, 증기 / 전기어려움 ( 장비대형 ) 기설치업체 ( 주 ) 새한미디어협조받음 국산 MVR 법경쟁우위성 일본제품 (S) 과 직접특성비교 - 증기압축기특성 : 회전수 3,600/25,000(rpm), 압축기직경 150/30(cm) -> 국산이크기 1/5, 회전속도 7배고속-> 소형, 초정밀제작, 고효율 - 에너지절약정도 : 국산열펌프성적계수 (COP)=23, 세계 Top class수준 -> 직접투입한에너지량의 23 배에너지를무료로얻어활용함. - 폐수처리단가 : 2,000( 원 / 톤 ) 미만, S사제품의 65(%) 수준 -> 국내타업체의 1/10 수준임. ( 참고 : 폐수위탁처리비 80,000( 원 / 톤 ) 수준 ) - 소음 : 정숙 - 이동성 : 6 미터콘테이너에내장가능토록형상최적화, 임의장소이동가능 - 모든핵심부품설계 / 제작 / 시험평가국내수행, 부품단가와 A/S비용최소화 - 추정장비가 : 일본의 60(%) 수준 P_30

Distiller Apparatus Is the distilled water from simple distiller apparatus identical with that of MVR distiller?

31 User s Preparation for Quality Check of Distilled Water Raw Water ( 원수 ) Steam ( 증기 ) How easily can we get the distilled water from questionable raw water to analyze quality? Distiller Apparatus Is the distilled water from simple distiller apparatus identical with that of MVR distiller? Yes, acceptably!! Based on the same principle. i Heat Source ( 열원 ) ( 증류장치 ) Water Cooler ( 물냉각기 ) Water Collector ( 수집기 ) Raw Water ( 원수 ) Electric Heater ( 온도조절용히터 ) P_31

32 MVR 응용시스템예 : LG 화학 개선전 옥탄올공정의 96 탑정증기중일부는탑정 CONDENSER에서냉각수로 78 까지냉각응축후 REFLUX로공급되고있었음. 개선후 증류탑탑정의 CONDENSER 에서냉각수로냉각중인 96 유체를 MVR로압축하여 REBOILER 열원으로사용하여시간당 8T/H의스팀을절감함. 개선항목 절감액 절감량 온실가스저감량 ( 백만원 / 년 ) (TOE/ 년 ) (tc/ 년 ) 증류탑 MVR 시스템 1,300 2,253 1, C/W C/W FEED FEED ENERGY MVR RECYCLE 125 STEAM 8 t/h 절감 STEAM P_32

33 MVR 관련뉴스거리 P_33

34 We hope to / can do work together in near future Turbo MVR Distiller Developing View Thank you!! Steam Compressor Developing View 장시간감사합니다. 앞으로에너지절약형고효율장비확산을위해 최선의노력을경주하겠습니다 P_34

35 심층 : 증발법과성적계수비교 증발법 : => 증기이용방법 : MSF( 다단플레쉬 ), ME( 다중효용 ), => 증기압축방법 : TVC( 열증기압축 ), MVR( 기계증기재압축 ) 특징비교 : - 에너지절약 : MVR>>TVC>ME>MSF - 성적계수상대비 : 60 : 5 : 2 : 1 -장비크기 : MVR<<TVC<ME<MSF ME, MSF? 증기가무료인곳 : 발전소 TVC? 증기가무료 / 염가인곳 : 발전소, 소각장 - 적정설비용량 : 대 MSF, 대중 ME, TVC, 소 (100 톤 / 일미만 )MVR - 소요에너지종류 : ( 증기 / 전기 ) MSF,ME,TVC ( 전기 ) MVR P_35

1

北地区青少年境研会 Международный детский симпозиум по проблемам экологии региона Северо-Восточной Азии. 1 2 5 6 7 9 1. 2. 11 12 13 13 14 15 16 . (Nature) 100.. 90%.. 3000 10% 385. 1 1, 500 2kg.........