- •Реферат
- •Введение
- •1 Описание объекта автоматизации
- •1.1 Описание технологии синтеза катализатора
- •1.1.1 Подготовка к синтезу
- •1.1.2 Стадия дозирования
- •1.1.3 Стадия термообработки
- •1.1.4Стадия промывки
- •1.1.5Стадия активации
- •1.1.6 Выгрузка магнийсодержащего носителя
- •1.1.7Подготовка к следующему синтезу
- •2 Задачи асу тп
- •2.1 Функции подсистемы
- •2.1.1 Измерение технологических параметров
- •2.1.2 Контроль технологических параметров и состояния оборудования
- •2.1.3 Автоматическое регулирование
- •2.1.4 Управление азотными режимами
- •2.1.5 Дозирование
- •2.2 Входные и выходные технологические параметры
- •2.2.1 Перечень входных параметров
- •2.2.2 Перечень выходных параметров
- •3 Программное обеспечение подсистемы синтеза катализатора опытного производства
- •3.1 Алгоритмы управления синтезом катализатора
- •3.1.1 Алгоритмы азотных режимов
- •3.1.2 Алгоритмы контроля
- •3.2 Алгоритмы регулирования
- •4 Технико-экономическое обоснование
- •4.1 Организация и планирование
- •4.1.1 Перечень работ
- •4.1.2 Загрузка исполнителей
- •4.1.3 Расчет трудоемкости этапов
- •4.2 Расчет сметы затрат на разработку
- •4.2.1 Расходы на материалы и покупные изделия
- •4.2.2 Основная заработная плата
- •4.2.3 Дополнительная заработная плата
- •4.2.4 Отчисления в социальные фонды
- •4.2.5 Расходы на оборудование для выполнения работ
- •4.2.6 Прочие прямые расходы
- •4.2.7 Накладные расходы
- •4.2.8 Расчет предполагаемой цены разработки
- •4.3 Расчет эффективности внедрения системы в производство
- •5 Безопастность и экологичность проекта
- •5.1 Анализ опасных и вредных факторов
- •5.1.1 Общие сведения
- •5.1.2 Анализ вредных и опасных производственных факторов
- •5.2 Производственная санитария
- •5.2.1 Требования эргономики и технической эстетики к рабочему месту инженера-программиста
- •5.2.2 Микроклимат рабочей среды
- •5.2.3 Нормативные требования к рабочему месту
- •5.2.4 Требования безопасности к излучению от дисплея
- •5.2.5 Шумоизоляция
- •5.2.6 Расчет искусственного освещения
- •5.3 Техника безопасности
- •5.3.1 Требования к элетробезопасности
- •5.4 Безопасность в чрезвычайных ситуациях
- •5.4.1 Пожарная профилактика
- •5.4.2 Оценка пожарной безопасности помещения
- •5.4.3 Анализ возможных причин возгорания
- •5.4.4 Мероприятия по устранению и предупреждению пожаров
- •5.5 Охрана окружающей среды
- •Заключение
- •Conclusion
- •Список использованных источников
- •Приложение 1. Description of automation object
- •1.1 Description of technology of synthesis of magnesium-bearing alloy
- •1.1.1 Preparation for synthesis
- •1.1.2 Stage of dispensing
- •1.1.3 Stage of heat treatment
- •1.1.4 Stage of washing
- •1.1.5 Stage of activation
- •1.1.6 Unloading magnesium-bearing alloy
- •1.1.7 Preparation for the next synthesis
1.1.5 Stage of activation
The activation stage is done for the preparation of the activated magnesium-bearing alloy.
In a laboratory of department 502, ethyl spirit is absolutised, and airtight calculated quantities of ethyl spirit are loaded under nitrogen into a portable container (pos. Х-301) preliminary ventilated by nitrogen, and representing a portable vertical vessel with capacity 0,002 m3. The container is equipped by a stationary siphon and connecting pipe with a stop valve for connecting through a flexible hose the pipelines of ventilation and nitrogen.
The reactor (pos. Р-302 (Р-402)) is used in the synthesis of the magnesium-bearing alloy in "pos. Р-301 (Р-302)" for the preparation of ethanol and TEOS solutions and dispensing activating solutions in the reactor with the magnesium-bearing alloy through the pump (pos. Н-303).
In the reactor (pos. Р-302 (Р-402)) is given the calculated quantity of heptane from "pos. М-311" or a returnable washing solution from "pos. Е-304/1". The ethanol from "pos. Х-301" is passed over through a flexible hose by nitrogen in "pos. Р-302 (Р-402)"; the mixer is switched on, and the mix is mixed for not less than 5 minutes.
After executing the third washing of the magnesium-bearing alloy in a reactor (pos. Р-301 (Р-302)) the additional portion of heptane from "pos. М-311" or a returnable washing solution from "pos. Е-304/2" is loaded. The system of temperature regulation is turned on and the reactor contents, while being mixed, are thermoestablished at temperature (10-15) оС during 0,5 hour. Then while mixing the suspension of the magnesium-bearing alloy in the reactor (pos. Р-301 (Р-302)) from "pos. Р-302 (Р-402)" through a diaphragm dosing pump (pos. Н-303) the ethanol solution is given. Dispensing is executed at a constant temperature during 1 hour. After the dispensing termination, the suspension of the magnesium-bearing alloy is carried out at (10-15) оС during 0,5 hour.
In the laboratory of department 502 airtight under nitrogen in the portable container (pos. Х-302), preliminary is ventilated by nitrogen, calculated quantities of TEOT are loaded.
The container (pos. Х-302) represents a portable vertical vessel with capacity 0,007 m3, equipped a stationary siphon and a connecting pipe with a stop valve for connection through a flexible hose of pipelines ventilation and nitrogen.
In the reactor (pos. Р-302 (Р-402)) a calculated quantity of heptane is passed from "pos. М-311" or a returnable washing solution from "pos. Е-304/2". After the washing solution from "pos. Е-304/2" has been sent, the pipeline of the returnable washing solution is ventilated by nitrogen from the reactor (pos. Р-301 (Р-302, Р-402)) through bypass (pos. FQIRSAH-304, HSA-304) in "pos. Е-304/2".
TEOT from "pos. Х-301" through a flexible hose is pressed over by nitrogen in reactor (pos. Р-302 (Р-402)), the mixer is switched on, and the mix is mixed for not less than 10 minutes.
While mixing the suspension of the magnesium-bearing alloy in the reactor (pos. Р-301 (Р-302)) from the reactor (pos. Р-302 (Р-402)) through a diaphragm dosing pump the solution of TEOT is given. Dispensing is executed at the constant temperature (10-15) оС during 1 hour.
After the termination of dispensing the solution TEOT, the even raising of temperature, 0,3 оС in a minute, is executed in the reactor (pos. Р-301 (Р-302)) from (10-15) оС to 30 оС during 1 hour.
Further, the reactionary mix is maintained during 2 hours at 30 оС.
Then with the switched-off mixer is executed, the sedimentation of the magnesium-bearing alloy during (30-40) minutes. After the sedimentation of the suspension of the magnesium-bearing alloy and decanting the liquid phase from the reactor (pos. Р-301 (Р-302)) into collection-container (pos. Е-303), the magnesium-bearing alloy is washed once by heptane at 30 оС (for the washing there is used pure heptane from "pos. Е-311"). After the sedimentation of suspension the washing solution is deleted in the collection (pos. Е-304/2), also is used repeatedly for the preparation of the suspension of the magnesium-bearing alloy for activation in "pos. Р-301 (Р-302)" and preparations of activating solutions in "pos. Р-302 (Р-402)".
The possibility of removal of washing solutions from "pos. Р-301 (Р-302)" is provided through a mobile siphon a filter. In this case the sedimentation of the suspension of the magnesium-bearing alloy is not executed, the reactor mixer is switched off and the mobile siphon falls to the bottom of the reactor. After that the washing solution through a filter, which has been built in a siphon is pressed over by nitrogen in "pos. Е-303" or in "pos. Е-304/2".
The collection-container of washing solutions (pos. Е-304/2) represents a vertical cylindrical device with capacity 1 m3, intended for gathering the washing solution after washing of the activated magnesium-bearing alloy with the following return to "pos. Р-301 (Р-302, Р-402)" as a solvent for the preparation of activation solutions and preparation of suspension of the magnesium-bearing alloy at the stage of activation of the next synthesis.
The possibility of clearing of "pos. Е-304/2" through the pump (pos. Н-304) in collection-container of washing solutions on external installation is provided, and also it is possible to have the recycle of the washing solution from "pos. Е-304/2" through the pump (pos. Н-304) with return to "pos. Е-304/2".
With the synthesis of the activated magnesium-bearing alloy, only the third washing at the stage of synthesis of the magnesium-bearing alloy is used again (through the container (pos. Е-304/1) it goes on the first washing of the magnesium-bearing alloy in the next synthesis). Washing of the activated magnesium-bearing alloy is used again in the next synthesis, which is gathered in the container (pos. Е-304/2) and is used for the preparation of suspension of the magnesium-bearing alloy in the reactor (pos. Р-301 (Р-302)) at the stage of activation and preparation of ethanol and TEOT solutions in "pos. Р-302 (Р-402)".
Washing with pure heptane "pos. Е-303, Е-304/1, Е-304/2" is provided as a variation.