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RU97116465A - PLANT FOR BIOCHEMICAL CLEANING OF HIGHLY CONCENTRATED WASTE WATERS - Google Patents

PLANT FOR BIOCHEMICAL CLEANING OF HIGHLY CONCENTRATED WASTE WATERS

Info

Publication number
RU97116465A
RU97116465A RU97116465/25A RU97116465A RU97116465A RU 97116465 A RU97116465 A RU 97116465A RU 97116465/25 A RU97116465/25 A RU 97116465/25A RU 97116465 A RU97116465 A RU 97116465A RU 97116465 A RU97116465 A RU 97116465A
Authority
RU
Russia
Prior art keywords
chamber
tank
clarified
pipe
water
Prior art date
Application number
RU97116465/25A
Other languages
Russian (ru)
Other versions
RU2139257C1 (en
Inventor
В.П. Колесников
В.Д. Климухин
Original Assignee
В.П. Колесников
В.Д. Климухин
ООО "Экосистема"
Filing date
Publication date
Application filed by В.П. Колесников, В.Д. Климухин, ООО "Экосистема" filed Critical В.П. Колесников
Priority to RU97116465A priority Critical patent/RU2139257C1/en
Priority claimed from RU97116465A external-priority patent/RU2139257C1/en
Priority to US09/509,845 priority patent/US6217759B1/en
Priority to PCT/RU1998/000126 priority patent/WO1999018038A1/en
Priority to CA 2305186 priority patent/CA2305186A1/en
Priority to EP19980929940 priority patent/EP1040083A1/en
Priority to AU79440/98A priority patent/AU7944098A/en
Publication of RU97116465A publication Critical patent/RU97116465A/en
Application granted granted Critical
Publication of RU2139257C1 publication Critical patent/RU2139257C1/en

Links

Claims (4)

1. Установка для биохимической очистки высококонцентрированных сточных вод, содержащая комбинированное устройство с биофильтром, аэротенком-отстойником, камерой смешения, циркуляционным насосом и технологическими трубопроводами, отличающаяся тем, что она снабжена биокоагулятором-флотатором первой ступени очистки с водоструйным аэратором, его приемной камерой и отражателем пены и трубопроводом отвода осветленной воды, биокоагулятором второй ступени очистки с водоструйным аэратором, его приемной камерой и трубопроводами отвода осветленной воды и осадка, биофильтром с промежуточной емкостью, сборными поддонами, аэрационными колоннами и реакционной емкостью с искусственной загрузкой, ферментатором с системой орошения, биофильтром, аэрационными колоннами, аэротенком-отстойником с искусственной загрузкой и циркуляционным насосом, трубопроводом отвода осветленных стоков и приемным резервуаром о двумя насосами для перекачки осветленных стоков,
напорный трубопровод циркуляционного насоса комбинированного устройства сообщен с промежуточной емкостью биофильтра и приемными камерами водоструйных аэраторов первой и второй ступеней очистки, напорный трубопровод первого насоса перекачки осветленных стоков соединен с приемной камерой аэратора первой ступени очистки, а напорный трубопровод второго насоса перекачки осветленных стоков - с промежуточной емкостью биофильтра, трубопровод отвода осветленных стоков от второй ступени очистки подключен к приемному резервуару, трубопровод отвода осадка от второй ступени очистки соединен с всасывающим трубопроводом насоса ферментатора, а напорный трубопровод этого насоса соединен с системой орошения ферментатора и приемными камерами аэраторов первой и второй ступени очистки и трубопровод отвода осветленной воды от ферментатора присоединен к приемному резервуару, а трубопровод отвода воды от комбинированного устройства подсоединен к биореактору доочистки стоков, снабженному камерой аэрации, искусственной загрузкой, перфорированными трубами, соединенными отводящими трубопроводами с циркуляционным насосом, напорный трубопровод которого подключен к приемной камере водоструйного аэратора.1. Installation for biochemical treatment of highly concentrated wastewater, containing a combined device with a biofilter, aeration tank-sump, a mixing chamber, a circulation pump and process piping, characterized in that it is equipped with a biocoagulator-flotator of the first treatment stage with a water-jet aerator, its receiving chamber and a reflector foam and clarified water drainage pipe, biocoagulator of the second cleaning stage with a water-jet aerator, its receiving chamber and drainage pipelines perishable water and sediment, a biofilter with an intermediate tank, prefabricated trays, aeration columns and a reaction tank with artificial loading, a fermenter with an irrigation system, a biofilter, aeration columns, an aeration tank with artificial loading and a circulation pump, a clarified sewage discharge pipe and a receiving tank two pumps for pumping clarified wastewater,
the pressure pipe of the circulation pump of the combined device is in communication with the intermediate tank of the biofilter and the receiving chambers of the water-jet aerators of the first and second cleaning stages, the pressure pipe of the first pump for pumping the clarified effluents is connected to the receiving chamber of the aerator of the first cleaning stage, and the pressure pipe of the second pump for pumping the clarified wastes with the intermediate tank biofilter, drainage pipe for clarified effluents from the second cleaning stage is connected to a receiving tank, pipelines The sediment discharge from the second purification stage is connected to the suction pipe of the fermenter pump, and the pressure pipe of this pump is connected to the fermenter irrigation system and the receiving chambers of the first and second purification aerators and the clarified water drain pipe from the fermenter is connected to the receiving tank, and the water drain pipe from the combined device is connected to the bioreactor of post-treatment of wastewater, equipped with an aeration chamber, artificial loading, perforated pipes connected to the discharge and pipes with circulation pump, the pressure line is connected to water jet aerator inlet chamber. 2. Установка по п. 1, отличающаяся тем, что биокоагулятор-флотатор выполнен из трех камер - камеры флотации, камеры отстаивания и камеры накопления осадка, при этом камера флотации снабжена лотком для сбора всплывающих веществ с отводным трубопроводом, аэраторами тонкого диспергирования воздуха и отделена от камеры осадка угoлкaми, полки которых установлены под углами наклона к горизонту 45-60 градусов. 2. Installation according to claim 1, characterized in that the biocoagulator-flotator is made up of three chambers - a flotation chamber, a settling chamber and a sediment accumulation chamber, while the flotation chamber is equipped with a tray for collecting pop-up substances with a bypass pipe, fine air dispersing aerators and is separated from the sediment chamber by corners, shelves of which are installed at angles of inclination to the horizon of 45-60 degrees. 3. Установка по п. 1, отличающаяся тем, что аэротенк ферментатора и реакционная емкость биофильтра снабжены искусственной загрузкой, состоящей из листов с равными диаметрами отверстий и равными расстояниями между щетинками, а отстойник комбинированного устройства и биореактор для доочистки стоков снабжены загрузкой, в которой диаметр отверстий и расстояния между щетинками уменьшаются от низа к верху листов. 3. Installation according to claim 1, characterized in that the aeration tank of the fermenter and the reaction tank of the biofilter are equipped with an artificial load consisting of sheets with equal hole diameters and equal distances between the bristles, and the sump of the combined device and the bioreactor for tertiary treatment of sewage are equipped with a load in which the diameter holes and the distance between the bristles are reduced from the bottom to the top of the sheets. 4. Установка по п. 1, отличающаяся тем, что пространства над аэрируемыми элементами сооружений закрыты герметично и для отвода воздуха к ним подсоединены воздуховоды, которые в свою очередь подключены к установке с бактерицидными лампами. 4. Installation according to claim 1, characterized in that the spaces above the aerated elements of the structures are closed hermetically and for the removal of air, air ducts are connected to them, which in turn are connected to the installation with bactericidal lamps.
RU97116465A 1997-10-03 1997-10-03 Plant for biochemical purification of very concentrated sewage RU2139257C1 (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
RU97116465A RU2139257C1 (en) 1997-10-03 1997-10-03 Plant for biochemical purification of very concentrated sewage
US09/509,845 US6217759B1 (en) 1997-10-03 1998-04-27 Installation for biochemical sewage treatment
PCT/RU1998/000126 WO1999018038A1 (en) 1997-10-03 1998-04-27 Installation for biochemichal sewage treatment
CA 2305186 CA2305186A1 (en) 1997-10-03 1998-04-27 Installation for biochemichal sewage treatment
EP19980929940 EP1040083A1 (en) 1997-10-03 1998-04-27 Installation for biochemichal sewage treatment
AU79440/98A AU7944098A (en) 1997-10-03 1998-04-27 Installation for biochemichal sewage treatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
RU97116465A RU2139257C1 (en) 1997-10-03 1997-10-03 Plant for biochemical purification of very concentrated sewage

Publications (2)

Publication Number Publication Date
RU97116465A true RU97116465A (en) 1999-07-10
RU2139257C1 RU2139257C1 (en) 1999-10-10

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
RU97116465A RU2139257C1 (en) 1997-10-03 1997-10-03 Plant for biochemical purification of very concentrated sewage

Country Status (6)

Country Link
US (1) US6217759B1 (en)
EP (1) EP1040083A1 (en)
AU (1) AU7944098A (en)
CA (1) CA2305186A1 (en)
RU (1) RU2139257C1 (en)
WO (1) WO1999018038A1 (en)

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