SU724462A1 - Method of hydrolysis yeast production waste water purification - Google Patents
Method of hydrolysis yeast production waste water purification Download PDFInfo
- Publication number
- SU724462A1 SU724462A1 SU782636035A SU2636035A SU724462A1 SU 724462 A1 SU724462 A1 SU 724462A1 SU 782636035 A SU782636035 A SU 782636035A SU 2636035 A SU2636035 A SU 2636035A SU 724462 A1 SU724462 A1 SU 724462A1
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- SU
- USSR - Soviet Union
- Prior art keywords
- waste water
- water purification
- production waste
- yeast production
- biological
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- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
Description
ПротокDuct
Объем заполнени Filling volume
ферментера Расход воздухаfermenter air flow
Ферментационна установка состоит из ферментера, снабженного мехажической мешалкой , системой воэдухораонределени - барбатером, блоком контрол рНГВлоком контрол и регул ции температуры, а также Системой ненрерывной подачи питательного субстрата (ПДБ) и отбора культуральной ЖИДКОСТ1И.The fermentation unit consists of a fermenter equipped with a mechanical agitator, a barbaterier air detection system, a barbater, a control unit with an LNG unit for temperature control and regulation, as well as a System for the continuous feeding of the nutrient substrate (PDB) and selection of the culture liquid.
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Темлературу культивировани поддерживают на уровне 3.7°C±jl°C, ,,4± ±0,2, продолжительность эксперимента 76 ч при времеии пребьгвайл .в ферментёре 3:ч. ;.The cultivation temperature is maintained at 3.7 ° C ± jl ° C ,, 4 ± 0.2, the duration of the experiment is 76 hours while the preservation in the fermenter is 3: h. ;.
Пример. Очистке подвергают последрожжевую бражку Красно рского биохимического завода. В качестве биоокислителей используют . омешанную культуру мироорганизмов вида Pseudobacterium sp, Lactobacterium reich и Micococcus alb.Example. The post-yeast brew of the Krasnoyarsk Biochemical Plant is subjected to cleaning. As bio-oxidants use. mixed culture of the microorganisms of the species Pseudobacterium sp, Lactobacterium reich and Micococcus alb.
Результаты экаперимента приведены в табл. 1..The results of the ekapimene are given in table. one..
На .основании полученных данных мо к но Вделать следующие выводы: степень очистки ПДБ смешанной культуроймикроорганизмов вида Pseudobacterium sp, Lactpbacterium leich и Micococcus alb достигает62 68% 1Ю Х1Ж(}ШШ Чб1Жбму потреблению кислорода): утилиза ци остаточных Сахаров составл ет 70-72,3 %.On the basis of the obtained data, one can draw the following conclusions: the degree of purification of PDB by a mixed culture of microorganisms of the species Pseudobacterium sp, Lactpbacterium leich and Micococcus alb reaches 62 68% 1Ü H1G (} ШШ Чб1ЖБмуму oxygen consumption): utilization of residual Sugars is 70-72.3 %
Таким образом, если при времени пребывани ПДБ вферментёре 1-1,5 ч эффектившсть очистки ПДБ грибной .микрофлорой не превышает 26% по ХПК и съем допол-ннтельной биомассы ие более 4,95 тн/сдт, то 11осле внедрени поликультуСравнительные данные по степени очистки последрбжжевой бражки при разных нагрузках по -потоку известным и предлагаемым способами приведены в табл. 2. Врем иребывани сточных, вод в ферментёре 1,0-1,5Ч.Thus, if with a residence time of a PDP in the enzyme of 1-1.5 hours, the effectiveness of cleaning the PDB with fungal microflora does not exceed 26% of COD and eat an additional biomass of more than 4.95 tons / sdt, then after the introduction of a polycult Comparative data on the degree of purification After-seasoning brazka at different loads on the flow of known and proposed methods are given in Table. 2. Time for wastewater recuperation, in the fermenter 1.0-1.5.
Таблица 2table 2
Биоокнсление последрожжевой бра.жкиBiooclination of the post-harvest bra.zhki
ры, состо щей из . Pseudobacterium sp, Lactobacterium leich и Micococcus alb эффективность очнстки достигает 41% по ХПК iH Съем допрлкительной биомассы увеличиваетс до 6,15 тн1 сутки.56rs consisting of. The pseudobacterium sp, Lactobacterium leich and Micococcus alb efficacy of freshness reaches 41% for COD iH. The removal of additional biomass increases to 6.15 tons per day.56
Формула и.з обретени тем, что стоечные воды подвергают обработ ( . .ке биологическим окислителем ,в течениеThe formula for the acquisition of the fact that the rack water is treated (.ke a biological oxidant, during
1.Способ очистки -сточных вод шдро-. 1-3. ч.1. The method of cleaning wastewater shdro-. 1-3. h
лиэно-дрожжевого производства, преиму-, i - ilieno-yeast production, advantage-, i - i
щественно последрожжевой бражки, от ор- Источники информации, прин тые воpost-harvest brew, from the OR- Sources of information received in
ганических соединений путем обработкивнимание при экспертизе:ganic compounds by processing attention during examination:
биологическим окислителем-,- от лич а ю -.. щийс тем, что, с щелью повышени сте- 1. Авторское (свидетельство JI1CCPbiological oxidizing agent -, - as distinct from the fact that, with an elevation slit 1. Copyright (certificate JI1CCP
пени очистки и количества биомассы, в ка-№ 562514, кл. С 02 С 5/10, 09.08.1977.penalties for cleaning and biomass, in ka-№ 562514, cl. From 02 to 5/10, 08/09/1977.
честве биологического окислител исполь-Ю 2. Каменный В. И., Галышева Л. Н.the biological oxidizer is used by Yu 2. Kamenny V. I., Galysheva L. N.
зуют смешанную культуру микроорганиз-Биоокисление поеледрожжевой бражки мов В1ида Pseudobacterium sp, Lactobacte- плесневыми и дрожженодобиыми грибами /mixed culture of microorganisms-Bio-oxidation of yeast brew of mov B1ida Pseudobacterium sp, Lactobacte- with mold and yeast-like fungi /
rium leih и Micococcus alb. в аппарате эрлифтного типа. - Реф. сб.rium leih and micococcus alb. in the apparatus of airlift type. - Ref. Sat
2.Спосо1б ио п. 1, отличающийс Гидролизное производство, 1976, № 1.2. Sposob i p. 1, characterized by Hydrolytic Production, 1976, no. 1.
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Claims (2)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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SU782636035A SU724462A1 (en) | 1978-06-30 | 1978-06-30 | Method of hydrolysis yeast production waste water purification |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU782636035A SU724462A1 (en) | 1978-06-30 | 1978-06-30 | Method of hydrolysis yeast production waste water purification |
Publications (1)
Publication Number | Publication Date |
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SU724462A1 true SU724462A1 (en) | 1980-03-30 |
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SU782636035A SU724462A1 (en) | 1978-06-30 | 1978-06-30 | Method of hydrolysis yeast production waste water purification |
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SU (1) | SU724462A1 (en) |
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1978
- 1978-06-30 SU SU782636035A patent/SU724462A1/en active
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