Студопедия
Случайная страница | ТОМ-1 | ТОМ-2 | ТОМ-3
АрхитектураБиологияГеографияДругоеИностранные языки
ИнформатикаИсторияКультураЛитератураМатематика
МедицинаМеханикаОбразованиеОхрана трудаПедагогика
ПолитикаПравоПрограммированиеПсихологияРелигия
СоциологияСпортСтроительствоФизикаФилософия
ФинансыХимияЭкологияЭкономикаЭлектроника

Sour Water Stripper Flowsheet

To Generate a Txy | Activity Coefficient | Лабораторная работа № 5. | Starting Aspen Plus | And Global Options | The Electrolyte Wizard | Chemistry | Reaction | Selecting Electrolyte Property Models | Properties |


Читайте также:
  1. B) Is watered
  2. Kastution Waters
  3. RECULTIVATION OF TECHNOGENIC TERRITORIES BY MEHODS OF PHYTOMELIORATION ON KUZMINSKI SANDS IN THE WATER MOUTH OF THE VARZUGA RIVER IN A POLAR REGION
  4. THE STUDY OF WATER PROTECTION PARTS IN FOREST BUFFER ZONE OF YUNTOLOVSKY RESERVE

The process flow diagram and operating conditions for this

simulation are shown in the Process Diagram: Sour Water Stripper.

Two feed streams, one containing sour water, the other steam, are

fed to a stripper to remove CO2, H2S, and NH3 from the sour water.

Use RadFrac to simulate the stripper.

SOURWAT

STEAM

BOTTOMS

VAPOR

Temperature = 190 F

Pressure = 15 psi

Total flow = 10,000 lb/hr

Mass fraction H2S = 0.001

Mass fraction NH3 = 0.001

Mass fraction CO2 = 0.001

Mass fraction H2O = 0.997

Pressure = 15 psi

Saturated vapor

Estimated H2O

flow rate = 2,000 lb/hr

Above

Stage 3

On Stage

5.0 ppm NH3

9 Theoretical stages + condenser

Pressure = 15 psi

Estimated molar reflux ratio = 25

Condenser temperature = 190 F

saturated vapor distillate

Process Diagram: Sour Water Stripper

The specifications for the column are:

• 10 theoretical stages total (includes one for the condenser)

• Distillate product as saturated vapor (partial condenser)

• Initial estimate for molar reflux ratio = 25

• No reboiler

• Feed stream SOURWAT above stage 3

• Feed stream STEAM on stage 10

• Column pressure of 15 psi (isobaric)

• Vary the reflux ratio and stream STEAM feed rate to achieve a

bottoms product with 5 ppm (mass) of NH3 and a condenser

temperature of 190° F

Getting Started - Electrolytes Modeling a Sour Water Stripper3-3


Дата добавления: 2015-08-20; просмотров: 52 | Нарушение авторских прав


<== предыдущая страница | следующая страница ==>
Examining Simulation Results| Chemistry

mybiblioteka.su - 2015-2024 год. (0.006 сек.)