SU557103A1 - Method for automatic control of hydrolysis process - Google Patents
Method for automatic control of hydrolysis processInfo
- Publication number
- SU557103A1 SU557103A1 SU2157815A SU2157815A SU557103A1 SU 557103 A1 SU557103 A1 SU 557103A1 SU 2157815 A SU2157815 A SU 2157815A SU 2157815 A SU2157815 A SU 2157815A SU 557103 A1 SU557103 A1 SU 557103A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- hydrolysis
- hydrolyzate
- control
- output
- cooking liquid
- Prior art date
Links
Landscapes
- Paper (AREA)
Description
1one
Изобретение относитс к области биохимической промышленности, точнее гидролизного производства и касаетс способа автоматического управлени процессом гидролиза .The invention relates to the field of the biochemical industry, more specifically to hydrolysis production, and relates to a method for automatically controlling the hydrolysis process.
Известны способы управлени процессом ги-дролиаа с помощью программного управлени l.Methods are known for controlling the hydrolysis process by means of software control l.
Из известных способов автоматического управлени процессом гидролиза наиболее близким к изобретению вл етс способ управлени с использованием программных задатчиков подачи на варку варо-гтп м .ицкости и отвода гидролизата 2.Of the known methods of automatic control of the hydrolysis process, the closest to the invention is the method of control using software supply control knobs for cooking boil-cooking gtr and removing hydrolyzate 2.
Недостатком STOto способа управлени про цессом гидролиза вл етс низка эффективность .Особенно этот недостаток про вл етс при плохой фильтрации загруженного сырь . Это приводит к увеличению перепада давлени между верхним и нижним уровн ми фильтрующего сло , вследствие чего возрастает его гидродинамическое сопротивление, происходит накопление варочной жидкости в гидролизаппарате и потер Сахаров.The disadvantage of the STOto method of controlling the hydrolysis process is low efficiency. Especially this disadvantage occurs when the loaded raw material is poorly filtered. This leads to an increase in pressure drop between the upper and lower levels of the filtering layer, as a result of which its hydrodynamic resistance increases, accumulation of the cooking liquid in the hydrolysis unit and loss of sugars occurs.
Целью изобретени вл етс повышение The aim of the invention is to increase
эффективности управлени и производительности гидролизаппарата.control efficiency and hydrolysis apparatus productivity.
Дл достижени этой цели регулирование подачи варочной жидкости и отвода гидролизата осуществл ют одновременно в зависимости от величины рассогласовани заданного и текущего значени перепада давлени между верхним и нижним уровн ми фильтрующего сло в гидролизаппарате.To achieve this goal, the regulation of the supply of cooking liquor and removal of the hydrolyzate is carried out simultaneously, depending on the magnitude of the mismatch between the set and the current value of the differential pressure between the upper and lower levels of the filter bed in the hydrolysis apparatus.
На чертеже дана схема устройства, где показаны: гидролизаппарат 1, датчики 2,3 давлени , блок 4 сравнени , делитель 5 сигнала , регул торы 6,7, исполнительные механизмы 8,9 , заслонки 10,11, установленные на лини х подачи варочной жидкости 12 и выдачи гидролизата 13.The drawing shows a diagram of the device, where the following is shown: hydrolyzer 1, pressure sensors 2.3, block 4 comparisons, signal divider 5, regulators 6.7, actuators 8.9, dampers 10.11 mounted on the cooking liquid supply lines 12 and dispensing hydrolyzate 13.
В качестве сигнала управлени принимают сигнал перепада давлени между верхним и нижним уровн ми фильтрующего сло , затем дел т его на два независимых сигнала, пропорциональных перепаду давлений, из которых один используетс дл регулировани подачи варочной жидкости, а другой - дл регулировани потока гидролизата.As a control signal, they receive a differential pressure signal between the upper and lower levels of the filter layer, then divide it into two independent signals proportional to the differential pressure, one of which is used to regulate the flow of cooking liquor and the other to regulate the flow of the hydrolyzate.
Claims (2)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU2157815A SU557103A1 (en) | 1975-07-15 | 1975-07-15 | Method for automatic control of hydrolysis process |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU2157815A SU557103A1 (en) | 1975-07-15 | 1975-07-15 | Method for automatic control of hydrolysis process |
Publications (1)
Publication Number | Publication Date |
---|---|
SU557103A1 true SU557103A1 (en) | 1977-05-05 |
Family
ID=20627121
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU2157815A SU557103A1 (en) | 1975-07-15 | 1975-07-15 | Method for automatic control of hydrolysis process |
Country Status (1)
Country | Link |
---|---|
SU (1) | SU557103A1 (en) |
-
1975
- 1975-07-15 SU SU2157815A patent/SU557103A1/en active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
SU557103A1 (en) | Method for automatic control of hydrolysis process | |
SU451740A1 (en) | Method for automatic control of process of saccharification of starch containing media | |
SU562298A1 (en) | Method of controlling the filtering process | |
SU429064A1 (en) | METHOD OF AUTOMATIC CONTROL OF POLYMERIZATION PROCESS OR ETHYLENE COPOLYMERIZATION | |
SU981353A1 (en) | Method for automatically controlling concentration of miscella in extraction apparatus with preliminary impregnation of extracted material with solvent | |
SU442186A1 (en) | The method of automatic control of the polymerization process | |
SU1713618A1 (en) | Method for automatic control of suspension dehydrating process | |
SU1054411A1 (en) | Method for automatically controlling liquid extraction in the production of antibiotics | |
SU654262A1 (en) | Apparatus for automatic regulation of complex fractionating column | |
SU1044704A1 (en) | Method of automatic control of purity of washing pulp mass in drum vacuum filters | |
SU507625A1 (en) | Method for automatic control of microbial cultivation process | |
SU858862A1 (en) | Extraction process automatic control method | |
SU889650A1 (en) | Device for automatic control of ethylbenzene two-step dehydrogenation process | |
SU1200942A1 (en) | Method of automatic control of a group of vacuum-filters operating in parallel | |
SU373256A1 (en) | ALL-UNION PATENT: "- ... LSH: AJ Oioliotena IBA | |
SU485748A1 (en) | The method of controlling the process of separating the suspension in a vacuum filter | |
SU680749A1 (en) | Method for controlling the operating conditions of a filtering plant | |
SU1055761A1 (en) | Method for automatically controlling reetherification of mixture of oils and fats on suspended alkali and alkali-earth metal alcoholates | |
GB2131182A (en) | A jig washbox control system | |
SU757620A1 (en) | Method of cellulose washing automatic control | |
SU1117279A1 (en) | Method of automatic control of phosphoric acid neutralization process | |
SU710564A1 (en) | Apparatus for automatic regulation of the duty of fractionating column of straight-run oil distillation apparatus | |
RU7617U1 (en) | FILTRATION AUTOMATIC CONTROL SYSTEM | |
SU922214A1 (en) | Method of automatic control of flushing unit with drum filters | |
SU798703A1 (en) | Multichannel adaptive controller |