WO2010050848A1 - Diaphragm pump - Google Patents
Diaphragm pump Download PDFInfo
- Publication number
- WO2010050848A1 WO2010050848A1 PCT/RU2009/000577 RU2009000577W WO2010050848A1 WO 2010050848 A1 WO2010050848 A1 WO 2010050848A1 RU 2009000577 W RU2009000577 W RU 2009000577W WO 2010050848 A1 WO2010050848 A1 WO 2010050848A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- salt water
- pressure
- diaphragm
- supplying
- side section
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Ceased
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B43/00—Machines, pumps, or pumping installations having flexible working members
- F04B43/02—Machines, pumps, or pumping installations having flexible working members having plate-like flexible members, e.g. diaphragms
- F04B43/06—Pumps having fluid drive
- F04B43/067—Pumps having fluid drive the fluid being actuated directly by a piston
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
- B01D61/06—Energy recovery
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2313/00—Details relating to membrane modules or apparatus
- B01D2313/24—Specific pressurizing or depressurizing means
- B01D2313/243—Pumps
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/08—Seawater, e.g. for desalination
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/131—Reverse-osmosis
Definitions
- the alleged invention relates to diaphragm pumps, more specifically to diaphragm pumps for supplying high-pressure salt water to a desalination plant of reverse osmosis plants for the purification and desalination of sea water.
- a diaphragm pump for supplying high-pressure salt water to a desalination plant, the internal cavity of the casing of which is divided by two symmetrically mounted flexible diaphragms into three insulated sections, the central of which is made with an input for receiving salt water and with an outlet for supplying salt water to the desalination plant, the side sections contain a liquid with a high viscosity, while a multiplier acting on a flexible diameter is installed in the first of the side sections Ragmi through the liquid with high viscosity, when exposed to the brine entering the first side section of the distiller.
- a disadvantage of the known high-pressure diaphragm pump for supplying salt water to the desalination plant is the presence of an hydraulic oil actuator acting on the flexible diaphragm, which complicates the design and increases its cost. Disclosure of invention
- the technical result achieved in the claimed invention is to simplify the design and operation, increase compactness and increase the reliability of the diaphragm pump, reducing its cost.
- a diaphragm pump for supplying high-pressure salt water to a desalination plant
- the internal cavity of the casing of which is divided by two symmetrically mounted flexible diaphragms into three isolated sections, the central of which is made with an input for receiving salt water and with an output for supplying salt water into desalination plant
- the side sections contain a liquid with a high viscosity, while in the first of the side sections there is a multiplier acting on the flexible diaphragm through the liquid be highly viscous, when exposed to the brine entering the first side section of the distiller, and the second side section of the plunger is mounted with the possibility of reciprocating movement and effects on the flexible diaphragm through the high viscosity liquid.
- the central section can be made with an inlet equipped with a valve for receiving salt water under a pressure of 2.3 kg / cm 2 and with an outlet equipped with a valve for supplying salt water to a desalination plant with a pressure of 59 kg / cm.
- FIG. 1 shows a schematic diagram of the claimed diaphragm pump for supplying high-pressure salt water to a desalination plant.
- the arrangement and operation of the claimed diaphragm pump is illustrated using the circuit shown in FIG. 1, taking into account its interaction with other devices that are part of the desalination plant reverse osmosis for the purification and desalination of sea water, including:
- the diaphragm pump 3 includes three diaphragms 6, a piston of the multiplier 7 and has a cavity B for salt water, cavity A for a liquid with a high viscosity, compressible pressure of about 60 kg / cm 2 , cavities B and D for a liquid with a high viscosity to transfer brine energy through diaphragm 6 to the plunger piston and further diaphragm 6 for supplying salt water.
- the internal cavity of the pump casing 3 is divided by two symmetrically mounted flexible diaphragms 6 into three isolated sections A, B, B.
- the central section B is connected at the inlet through a check valve 2 with a salt water supply device 1 under a pressure of 2.3 - - .2.5 kg / cm 2 , and at the outlet through a non-return valve 8 with a pressure of 59 ... 60 kg / cm 2 with an inlet 9 into the desalination unit 10.
- Side section A is connected to the plunger 4 with cyclic compression from the fluid drive 5 to a pressure of 59 ... 60 kg / cm 2 .
- the actuator 5 can be made in the form of a cam mechanism or a crank mechanism that provides a cyclic reciprocating movement of the plunger 4.
- the lateral section B through the multiplier 7 is connected to the distribution valve of the brine 13 connected to the drain 14 and to the desalination unit 10.
- the diaphragm pump 3 with the multiplier 7 increases the pressure of the brine leaving the desalination plant 10 to 59 ... 60 kg / cm.
- the brine after the distributor 13 falls periodically into the side section D of the high-pressure pump 3, acting on the third diaphragm 6, which is located in the pump casing 3 between the cavities G and D, or on the drain 14.
- the ratio of the squares of the larger and smaller diameter of the multiplier piston is equal to the ratio of the pressures in salt water pressure line 9 and brine line 12.
- Desalination plant reverse osmosis works as follows. From the pipeline 1, through the check valve 2, salt water enters the cavity B of the hydraulic cylinder and bends outward of the diaphragm 6. After filling the cavity B with water, a sufficient force is applied to create the osmotic pressure in the membrane elements of the desalination unit 10, and a brine under high pressure from past cycles and presses on the plunger piston and diaphragm 6.
- Cavities A, B, D filled with a high-viscosity fluid transmit pressure, and diaphragms 6 in cavity B pump salt water under high pressure through the check valve 8 into the pipeline 9.
- Part of the water is supplied by moving the plunger 4, and the other part by moving the piston of the multiplier 7.
- Water from the pipe 9 enters the membrane elements of the desalination unit 10 and through the pipe 11 the desalinated water leaves the installation.
- the brine formed during desalination under high pressure enters the pipeline 12 and from it into the distribution valve of the brine 13, through which, during injection, the brine under high pressure is fed into the cavity D.
- the brine from the cavity D is discharged through valve 13 into the pipeline fourteen.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Water Supply & Treatment (AREA)
- Nanotechnology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
Диафрагменный насос Diaphragm pump
Область техникиTechnical field
Предполагаемое изобретение относится к диафрагменным насосам, более точно к диафрагменным насосам для подачи соленой воды под высоким давлением в опреснитель установок обратного осмоса для очистки и опреснения морской воды.The alleged invention relates to diaphragm pumps, more specifically to diaphragm pumps for supplying high-pressure salt water to a desalination plant of reverse osmosis plants for the purification and desalination of sea water.
Предшествующий уровень техники Известен, заявка JVf-! 2007109399, опубликованная 20.09.2008, и заявка N°2007130523, опубликованная 20.02.2009, диафрагменный насос для подачи соленой воды под высоким давлением в опреснитель, внутренняя полость корпуса которого разделена двумя симметрично установленными гибкими диафрагмами на три изолированные секции, центральная из которых выполнена с входом для приема соленой воды и с выходом для подачи соленой воды в опреснитель, боковые секции содержат жидкость с высокой вязкостью, при этом в первой из боковых секций установлен мультипликатор, воздействующий на гибкую диафрагму через жидкость с высокой вязкостью, при воздействии на него рассола, поступающего в первую боковую секцию из опреснителя.BACKGROUND OF THE INVENTION JVf-! 2007109399, published on September 20, 2008, and application N ° 2007130523, published on February 20, 2009, a diaphragm pump for supplying high-pressure salt water to a desalination plant, the internal cavity of the casing of which is divided by two symmetrically mounted flexible diaphragms into three insulated sections, the central of which is made with an input for receiving salt water and with an outlet for supplying salt water to the desalination plant, the side sections contain a liquid with a high viscosity, while a multiplier acting on a flexible diameter is installed in the first of the side sections Ragmi through the liquid with high viscosity, when exposed to the brine entering the first side section of the distiller.
Недостатком известного диафрагменного насоса высокого давления для подачи соленой воды в опреснитель является наличие масляного гидропривода, воздействующего на гибкую диафрагму, что усложняет конструкцию и увеличивает ее стоимость. Раскрытие изобретенияA disadvantage of the known high-pressure diaphragm pump for supplying salt water to the desalination plant is the presence of an hydraulic oil actuator acting on the flexible diaphragm, which complicates the design and increases its cost. Disclosure of invention
Техническим результатом, достигаемым в заявленном изобретении, является упрощение конструкции и эксплуатации, увеличение компактности и повышение надежности работы диафрагменного насоса, снижение его стоимости.The technical result achieved in the claimed invention is to simplify the design and operation, increase compactness and increase the reliability of the diaphragm pump, reducing its cost.
Указанные технические результаты достигаются в диафрагменном насосе для подачи соленой воды под высоким давлением в опреснитель, внутренняя полость корпуса которого разделена двумя симметрично установленными гибкими диафрагмами на три изолированные секции, центральная из которых выполнена с входом для приема соленой воды и с выходом для подачи соленой воды в опреснитель, боковые секции содержат жидкость с высокой вязкостью, при этом в первой из боковых секций установлен мультипликатор, воздействующий на гибкую диафрагму через жидкость с высокой вязкостью, при воздействии на него рассола, поступающего в первую боковую секцию из опреснителя, а во второй боковой секции установлен плунжер с возможностью его возвратно- поступательного движения и воздействия на гибкую диафрагму через жидкость с высокой вязкостью. Центральная секция может быть выполнена с входом, снабженным клапаном для приема соленой воды под давлением от 2,3 кг/см2 и с выходом, снабженным клапаном для подачи соленой воды в опреснитель с давлением от 59 кг/см .The indicated technical results are achieved in a diaphragm pump for supplying high-pressure salt water to a desalination plant, the internal cavity of the casing of which is divided by two symmetrically mounted flexible diaphragms into three isolated sections, the central of which is made with an input for receiving salt water and with an output for supplying salt water into desalination plant, the side sections contain a liquid with a high viscosity, while in the first of the side sections there is a multiplier acting on the flexible diaphragm through the liquid be highly viscous, when exposed to the brine entering the first side section of the distiller, and the second side section of the plunger is mounted with the possibility of reciprocating movement and effects on the flexible diaphragm through the high viscosity liquid. The central section can be made with an inlet equipped with a valve for receiving salt water under a pressure of 2.3 kg / cm 2 and with an outlet equipped with a valve for supplying salt water to a desalination plant with a pressure of 59 kg / cm.
Краткое описание чертежейBrief Description of the Drawings
Ha фиг. 1 показана принципиальная схема заявленного диафрагменного насоса для подачи соленой воды под высоким давлением в опреснитель. Осуществление изобретенияHa FIG. 1 shows a schematic diagram of the claimed diaphragm pump for supplying high-pressure salt water to a desalination plant. The implementation of the invention
Устройство и работа заявленного диафрагменного насоса поясняется с использованием схемы, приведенной на фиг. 1, с учетом его взаимодействия с другими устройствами, входящими в состав опреснительной установки обратного осмоса для очистки и опреснения морской воды, включающей:The arrangement and operation of the claimed diaphragm pump is illustrated using the circuit shown in FIG. 1, taking into account its interaction with other devices that are part of the desalination plant reverse osmosis for the purification and desalination of sea water, including:
1 - трубопровод подачи соленой воды под низким давлением, около 2,5 кг/см2); 2 - вход с обратным клапаном в центральную секцию;1 - pipeline supply of salt water under low pressure, about 2.5 kg / cm 2 ); 2 - entrance with a check valve into the central section;
3 - диафрагменный насос высокого давления;3 - diaphragm high pressure pump;
4 - плунжер;4 - a plunger;
5 - привод плунжера;5 - plunger drive;
6 - диафрагмы; 7 - поршень мультипликатора;6 - aperture; 7 - multiplier piston;
8 - выход с обратным клапаном из центральной секции;8 - exit with a check valve from the central section;
9 - трубопровод подачи соленой воды высокого давления;9 - pipeline supply of salt water of high pressure;
10 - блок мембранных элементов (опреснитель);10 - a block of membrane elements (desalination);
11 - трубопровод отвода опресненной воды; 12 - трубопровод отвода рассола с высоким давлением;11 - pipeline desalination of desalinated water; 12 - high pressure brine outlet pipe;
13 - клапан распределения рассола;13 - valve distribution of brine;
14 - трубопровод отвода рассола.14 - brine discharge pipe.
Диафрагменный насос 3 включает три диафрагмы 6, поршень мультипликатора 7 и имеет полость Б для соленой воды, полость А для жидкости с высокой вязкостью, сжимаемой давлением около 60 кг/см2 , полости В и Г для жидкости с высокой вязкостью для передачи энергии рассола через диафрагму 6 к поршню мультипликатора и дальше диафрагме 6 подачи соленой воды. Внутренняя полость корпуса насоса 3 разделена двумя симметрично установленными гибкими диафрагмами 6 на три изолированные секции А, Б, В. Центральная секция Б связана на входе через обратный клапан 2 с устройством 1 подачи соленой воды под давлением 2,3 - - .2,5 кг/см2, а на выходе через обратный клапан 8 с давлением 59...60 кг/см2 с входом 9 в опреснитель 10. Боковая секция А связана с плунжером 4 с циклическим сжатием от привода 5 жидкости до давления 59...60 кг/см2. Привод 5 может быть выполнен в виде кулачкового механизма или кривошипного механизма, обеспечивающего циклическое, возвратно-поступательное движение плунжера 4. Боковая секция В через мультипликатор 7 связана с клапаном распределения рассола 13, соединенным со сливом 14 и с опреснителем 10. Диафрагменный насос 3 с мультипликатором 7 повышает давление рассола, выходящего из опреснителя 10 до 59...60 кг/см . Рассол после распределителя 13 попадает периодически в боковую секцию Д насоса 3 высокого давления, воздействуя на третью диафрагму 6, которая находится в корпусе насоса 3 между полостями Г и Д, или на слив 14. Отношение квадратов большего и меньшего диаметра поршня мультипликатора равно отношению давлений в напорной линии соленой воды 9 и линии 12 рассола. D2. Всоленой воды 60 = 1,053 для среднесоленой морской воды,The diaphragm pump 3 includes three diaphragms 6, a piston of the multiplier 7 and has a cavity B for salt water, cavity A for a liquid with a high viscosity, compressible pressure of about 60 kg / cm 2 , cavities B and D for a liquid with a high viscosity to transfer brine energy through diaphragm 6 to the plunger piston and further diaphragm 6 for supplying salt water. The internal cavity of the pump casing 3 is divided by two symmetrically mounted flexible diaphragms 6 into three isolated sections A, B, B. The central section B is connected at the inlet through a check valve 2 with a salt water supply device 1 under a pressure of 2.3 - - .2.5 kg / cm 2 , and at the outlet through a non-return valve 8 with a pressure of 59 ... 60 kg / cm 2 with an inlet 9 into the desalination unit 10. Side section A is connected to the plunger 4 with cyclic compression from the fluid drive 5 to a pressure of 59 ... 60 kg / cm 2 . The actuator 5 can be made in the form of a cam mechanism or a crank mechanism that provides a cyclic reciprocating movement of the plunger 4. The lateral section B through the multiplier 7 is connected to the distribution valve of the brine 13 connected to the drain 14 and to the desalination unit 10. The diaphragm pump 3 with the multiplier 7 increases the pressure of the brine leaving the desalination plant 10 to 59 ... 60 kg / cm. The brine after the distributor 13 falls periodically into the side section D of the high-pressure pump 3, acting on the third diaphragm 6, which is located in the pump casing 3 between the cavities G and D, or on the drain 14. The ratio of the squares of the larger and smaller diameter of the multiplier piston is equal to the ratio of the pressures in salt water pressure line 9 and brine line 12. D 2 . Salted water 60 = 1,053 for medium salted sea water,
U "рассола Э ' гдеU 'brine e' where
D - больший диаметр поршня мультипликатора; d - меньший диаметр поршня мультипликатора; Рсоленои воды — давление в линии 9 подачи соленой воды к опреснителю; Ррассола- давление в линии 12 отвода рассола от опреснителя. Опреснительная установка обратного осмоса работает следующим образом. Из трубопровода 1 через обратный клапан 2 соленая вода поступает в полость Б гидроцилиндра и выгибает наружу диафрагмы 6. После заполнения полости Б водой к плунжеру 4 прикладывается усилие, достаточное для создания осмотического давления в мембранных элементах опреснителя 10, а в полость Д поступает рассол под высоким давлением от прошлых циклов и давит на поршень мультипликатора и диафрагму 6. Полости А, В, Г, заполненные жидкостью с высокой вязкостью, передают давление, и диафрагмами 6 в полости Б производится нагнетание соленой воды под высоким давлением через обратный клапан 8 в трубопровод 9. Часть воды подается перемещением плунжера 4, а другая часть перемещением поршня мультипликатора 7. Вода из трубопровода 9 поступает в мембранные элементы опреснителя 10 и через трубопровод 11 опресненная вода покидает установку. Образовавшийся во время опреснения рассол под высоким давлением поступает в трубопровод 12 и из него в клапан распределения рассола 13, через который во время нагнетания рассол под высоким давлением подается в полость Д. При заполнении полости Б водой рассол из полости Д сливается через клапан 13 в трубопровод 14. D is the larger diameter of the multiplier piston; d is the smaller diameter of the multiplier piston; Brine water - pressure in the line 9 of the salt water supply to the desalination plant; P brine - pressure in line 12 of the brine outlet from the desalination plant. Desalination plant reverse osmosis works as follows. From the pipeline 1, through the check valve 2, salt water enters the cavity B of the hydraulic cylinder and bends outward of the diaphragm 6. After filling the cavity B with water, a sufficient force is applied to create the osmotic pressure in the membrane elements of the desalination unit 10, and a brine under high pressure from past cycles and presses on the plunger piston and diaphragm 6. Cavities A, B, D filled with a high-viscosity fluid transmit pressure, and diaphragms 6 in cavity B pump salt water under high pressure through the check valve 8 into the pipeline 9. Part of the water is supplied by moving the plunger 4, and the other part by moving the piston of the multiplier 7. Water from the pipe 9 enters the membrane elements of the desalination unit 10 and through the pipe 11 the desalinated water leaves the installation. The brine formed during desalination under high pressure enters the pipeline 12 and from it into the distribution valve of the brine 13, through which, during injection, the brine under high pressure is fed into the cavity D. When filling the cavity B with water, the brine from the cavity D is discharged through valve 13 into the pipeline fourteen.
Claims
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| RU2008142403 | 2008-10-27 | ||
| RU2008142403 | 2008-10-27 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2010050848A1 true WO2010050848A1 (en) | 2010-05-06 |
Family
ID=42129033
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/RU2009/000577 Ceased WO2010050848A1 (en) | 2008-10-27 | 2009-10-27 | Diaphragm pump |
Country Status (2)
| Country | Link |
|---|---|
| RU (1) | RU94221U1 (en) |
| WO (1) | WO2010050848A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103075328A (en) * | 2013-01-25 | 2013-05-01 | 沈阳大学 | Hydrodynamic diaphragm pump |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| PL158515B1 (en) * | 1989-02-22 | 1992-09-30 | Membrane-type high-pressure pump | |
| RU2311559C2 (en) * | 2003-05-16 | 2007-11-27 | Уоннер Инджиниринг, Инк. | Diaphragm pump |
| WO2008121030A2 (en) * | 2007-03-15 | 2008-10-09 | Obshchestvo S Ogranichennoj Otvetstvennost'yu 'tehnoprom' | Reverse osmosis freshwater plant (variants) |
-
2009
- 2009-10-27 RU RU2009148105/22U patent/RU94221U1/en not_active IP Right Cessation
- 2009-10-27 WO PCT/RU2009/000577 patent/WO2010050848A1/en not_active Ceased
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| PL158515B1 (en) * | 1989-02-22 | 1992-09-30 | Membrane-type high-pressure pump | |
| RU2311559C2 (en) * | 2003-05-16 | 2007-11-27 | Уоннер Инджиниринг, Инк. | Diaphragm pump |
| WO2008121030A2 (en) * | 2007-03-15 | 2008-10-09 | Obshchestvo S Ogranichennoj Otvetstvennost'yu 'tehnoprom' | Reverse osmosis freshwater plant (variants) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103075328A (en) * | 2013-01-25 | 2013-05-01 | 沈阳大学 | Hydrodynamic diaphragm pump |
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| Publication number | Publication date |
|---|---|
| RU94221U1 (en) | 2010-05-20 |
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