SU1227604A1 - Method of ferment stabilization of organic deposit - Google Patents
Method of ferment stabilization of organic deposit Download PDFInfo
- Publication number
- SU1227604A1 SU1227604A1 SU807771535A SU7771535A SU1227604A1 SU 1227604 A1 SU1227604 A1 SU 1227604A1 SU 807771535 A SU807771535 A SU 807771535A SU 7771535 A SU7771535 A SU 7771535A SU 1227604 A1 SU1227604 A1 SU 1227604A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- stabilization
- enzymes
- mixture
- sludge
- amount
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
- C02F3/342—Biological treatment of water, waste water, or sewage characterised by the microorganisms used characterised by the enzymes used
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- Life Sciences & Earth Sciences (AREA)
- Microbiology (AREA)
- Biodiversity & Conservation Biology (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Treatment Of Sludge (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Enzymes And Modification Thereof (AREA)
- Paper (AREA)
Description
Изобретение относитс к способам ферментативной стаб лизацни органических осадков, в частности ила.The invention relates to methods for enzymatic stabilization of organic sediments, in particular sludge.
Известны дл обработки органических осадков аэробные и анаэробные способы. При аэробных способах обрабатываемый осадок аэрируют, чтобы обеспечить микробиологические процессы деструкции, протекающие только в присутствии кислорода. Врем вьщержки исходного материала 2,5-7 сут.Aerobic and anaerobic methods are known for treating organic sediments. With aerobic methods, the treated sediment is aerated to ensure microbiological processes of destruction that take place only in the presence of oxygen. The time lag of the source material is 2.5-7 days.
Анаэробные способы требуют значительно большего времени. Они протекают в отсутствии кислорода. Врем вьщержки 30-70 дней (см. И,С. Туровский . Обработка осадков сточных вод. М. Стройиздат, 1975, с, 32-35). Наиболее близким к предлагаемому по технической сущности и достигаемому результату вл етс способ фер- ментативнор стабилизации ила, включающий введение смеси ферментов, содержаощх амилазу, протеазу, глю- каназу, в исходный ил, перемеши- . вание и вьщерживание при 25-40 С. рН 5-8 в течение 5-10 ч с последующим разделением на стабилизированный ип и иловую воду (см. Патент ГДР № 140244, кл. С 02 F 11/12, 1978).Anaerobic methods require significantly more time. They flow in the absence of oxygen. The settlement time is 30-70 days (see I, S. Turovsky. Sludge treatment. M. Stroyizdat, 1975, p. 32-35). The closest to the proposed technical essence and the achieved result is a method of enzyme stabilization of sludge, including the introduction of a mixture of enzymes containing amylase, protease, glucanase, into the original sludge, mix- ing. and holding at 25–40 C. pH 5–8 for 5–10 h, followed by separation into stabilized SP and sludge water (see GDR Patent No. 140244, class C 02 F 11/12, 1978).
Целью изобретени вл етс повышение степени стабилизации и уменьЕпе ние потребности в ферментах.The aim of the invention is to increase the degree of stabilization and reduce the need for enzymes.
Способ осуществл ют следующим образом.The method is carried out as follows.
Провод т стабилизацию осадка путе введени смеси ферментов и в к -чест- ве комплексообразовател - динатрий- дигидрогенэтилендиаминтетраацетат. Смесь перемешивают и выдерживают при температуре предпочтительно 10-50 С рН 5-8, в течение предпочтительно 0,5-15 ч. Комплексообразователь ввод т предпочтительно в количествеSediment stabilization is carried out by introducing a mixture of enzymes and, in the cation complexing agent, disodium dihydrogen ethylene diamine tetraacetate. The mixture is stirred and maintained at a temperature of preferably 10-50 ° C pH 5-8, for preferably 0.5-15 hours. The complexing agent is preferably introduced in the amount of
Составитель Г„ Лебедева Редактор Н. Горват Техред Н.БонкалоCompiled by G. Lebedeva Editor N. Gorvat Tehred N. Bonkalo
Заказ 2257/24 Тираж 864ПодписноеOrder 2257/24 Circulation 864 Subscription
ВНИИПИ Государственного комитета СССРVNIIPI USSR State Committee
по делам изобретений и открытий 113035, Москва, Ж-35, Раушска наб. ,. д. 4/5for inventions and discoveries 113035, Moscow, Zh-35, Raushsk nab. , 4/5
Производственно-полиграфическое предпри тие, г. Ужгород, ул. Проектна , 4Production and printing company, Uzhgorod, st. Project, 4
33
35-70% от количества фермента. Смесь раздел ют на стабилизированный ил и иловую воду. Расход ферментов при этом значительно снижаетс .35-70% of the amount of enzyme. The mixture is divided into stabilized sludge and sludge water. The consumption of enzymes is significantly reduced.
Ферменты и Комплексообразователь примен ют преимущественно дл смесей 1-1.ГЮВ, состо щих из первичного и активного ила.Enzymes and complexing agents are used primarily for mixtures of 1-1. HEW, consisting of primary and active sludge.
Количество ферментов уменьшаетс приблизительно на 90% по сравнению со способом ферментативной стабилизации ила без комплексообразовател .The amount of enzymes is reduced by approximately 90% compared with the method of enzymatic stabilization of sludge without a complexing agent.
П р им е р. Освобожденный от грубых примесей первичный ил смешивают с избыточнь м илом процесса биологической очистки в отношении 1:5, ввод т смесь ферментов, содержащих амилазу , протеазу, глюканазу из расчета 0 на 1 м 3-10 г и комплексообразова- тель динатрийдигидрогенэтилендиамин- тетраацетат в количестве 35-70% от количества фермента, перемешивают - и выдерживают при 25 С 5 ч при сла- S бой аэрации с последующим гравитационным разделением на стабилизированный 1-ш и 1шовую воду.PRI im p The primary sludge freed from coarse impurities is mixed with an excess of 1: 5 biological purification process, a mixture of enzymes containing amylase, protease, glucanase at the rate of 0 per m 3-10 g and the complexing agent disodium dihydrogen ethylene diamine tetraacetate in the amount 35-70% of the amount of the enzyme is mixed - and kept at 25 C for 5 hours with weak S aeration followed by gravitational separation into stabilized 1-sh and 1show water.
Стабилизированный ил перенос т на иловую площадку дл сушки. Илова вода, содержаща питательные вещества , находит либо специальное применение , либо переводитс в аэротенк.The stabilized sludge is transferred to a sludge drying platform. The nutrient-containing water is either used for special purposes or is converted to an aeration tank.
При добавлении 0,5 г комплексообразовател /кг твердой фазы осадка количество фермента сокращаетс в 4 раза. Если прин ть разложение органического вещества без комплексообразовател за 100%, то разложение с комплексообразователен 170%.When adding 0.5 g of complexing agent / kg of solid sediment, the amount of enzyme is reduced by 4 times. If we take the decomposition of organic matter without the complexing agent for 100%, then the decomposition with the complexing agent is 170%.
Удельное сопротивление фильтрации стабилизированного осадка без комп (2The resistivity of the filtration of stabilized sediment without comp (2
лексообразовател 0,5-3-10 см, а с комплексообразователем 0,1 0lex former 0.5-3-10 cm, and with complexing agent 0.1 0
5five
00
2 12 1
1212
СМCM
Корректор С.ШекмарProofreader S. Shekmar
Claims (3)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DD21832780A DD157965A3 (en) | 1980-01-07 | 1980-01-07 | PROCESS FOR ENZYMATIC SLUDGE STABILIZATION |
Publications (1)
Publication Number | Publication Date |
---|---|
SU1227604A1 true SU1227604A1 (en) | 1986-04-30 |
Family
ID=5522154
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU807771535A SU1227604A1 (en) | 1980-01-07 | 1980-12-17 | Method of ferment stabilization of organic deposit |
Country Status (6)
Country | Link |
---|---|
AT (1) | AT388908B (en) |
BG (1) | BG34816A1 (en) |
CS (1) | CS258401B1 (en) |
DD (1) | DD157965A3 (en) |
DE (1) | DE3045712A1 (en) |
SU (1) | SU1227604A1 (en) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3441690A1 (en) * | 1984-11-15 | 1986-05-15 | VEB Projektierung Wasserwirtschaft, DDR-4020 Halle | Process for the enzymatic treatment of organic substances and biomass |
DE3443364A1 (en) * | 1984-11-28 | 1986-05-28 | FALI Landwirtschaftliche Service GmbH, 7867 Wehr | SOURCE TREATMENT AGENTS FOR PREVENTING FLOATING CEILINGS AND SINK LAYERS AND THE USE THEREOF |
DE3545321C2 (en) * | 1985-12-20 | 1995-07-20 | Gfs Ges Fuer Flugaschenverwert | Process for the treatment of sludges containing heavy metals |
CS275735B6 (en) * | 1988-09-14 | 1992-03-18 | Projekt Wasserwirtschaft Veb | Method of mesophilic or thermophilic anaerobic enzymatic conditioning of liquid organic substances and biological materials |
DE10249081A1 (en) * | 2002-10-21 | 2004-04-29 | Volker Lenski | Simplified sewage sludge treatment comprises an enzyme treatment step, and optionally a peroxide treatment step at an acidic pH |
SE531167C2 (en) * | 2007-05-31 | 2009-01-07 | Kemira Oyj | Process for treating sludge in water treatment |
CN108585438A (en) * | 2018-04-17 | 2018-09-28 | 沈阳环境科学研究院 | A kind of preparation method of sludge drying co-substrate fermentate |
-
1980
- 1980-01-07 DD DD21832780A patent/DD157965A3/en not_active IP Right Cessation
- 1980-12-01 BG BG8049938A patent/BG34816A1/en unknown
- 1980-12-04 AT AT592480A patent/AT388908B/en not_active IP Right Cessation
- 1980-12-04 DE DE19803045712 patent/DE3045712A1/en active Granted
- 1980-12-11 CS CS876980A patent/CS258401B1/en unknown
- 1980-12-17 SU SU807771535A patent/SU1227604A1/en active
Also Published As
Publication number | Publication date |
---|---|
DE3045712C2 (en) | 1989-04-20 |
AT388908B (en) | 1989-09-25 |
ATA592480A (en) | 1989-02-15 |
BG34816A1 (en) | 1983-12-15 |
CS258401B1 (en) | 1988-08-16 |
DD157965A3 (en) | 1982-12-22 |
DE3045712A1 (en) | 1981-10-22 |
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