Javascript must be enabled to continue!
Automatic determination of optimal endpoint of 1st carbonatation – factory trials
View through CrossRef
The objective of this paper is to determine the applicability of automatic control of the optimal point in 1st carbonatation of juice purification in a beet sugar factory. To realize the automated determination, a pilot carbonatation tank was constructed and installed in the bypass of the industrial production. Automatic stepwise carbonatation was applied to the circulation juice of the 1st carbonatation. pH value measurement started at a pH value of the circulation juice of approximately 12, and carbonatation gas was injected until the pH reached 10.7 in 0.1–0.2 pH units per step by means of an automatic control system. After every pH step, juice was left to settle for 4min. At the end of this clarification time, turbidity measurement was done. In total carbonatation, sedimentation and turbidity measurement take approximately 45–50min. When the period was completed, the tank was discharged and automatically washed out by extraction feed water. Data obtained at the end of the period were recorded and displayed on a personal computer. The computer software prepared for this system compares all the turbidity values, chooses the lowest one and designates the corresponding pH value at that turbidity as the optimal pH.
Title: Automatic determination of optimal endpoint of 1st carbonatation – factory trials
Description:
The objective of this paper is to determine the applicability of automatic control of the optimal point in 1st carbonatation of juice purification in a beet sugar factory.
To realize the automated determination, a pilot carbonatation tank was constructed and installed in the bypass of the industrial production.
Automatic stepwise carbonatation was applied to the circulation juice of the 1st carbonatation.
pH value measurement started at a pH value of the circulation juice of approximately 12, and carbonatation gas was injected until the pH reached 10.
7 in 0.
1–0.
2 pH units per step by means of an automatic control system.
After every pH step, juice was left to settle for 4min.
At the end of this clarification time, turbidity measurement was done.
In total carbonatation, sedimentation and turbidity measurement take approximately 45–50min.
When the period was completed, the tank was discharged and automatically washed out by extraction feed water.
Data obtained at the end of the period were recorded and displayed on a personal computer.
The computer software prepared for this system compares all the turbidity values, chooses the lowest one and designates the corresponding pH value at that turbidity as the optimal pH.
Related Results
IMPLEMENTASI TEACHING FACTORY DI SMKN 2 GEDANGSARI GUNUNGKIDUL
IMPLEMENTASI TEACHING FACTORY DI SMKN 2 GEDANGSARI GUNUNGKIDUL
Abstract. Evaluation of ‘teaching factory’ implementation in SMKN2 Gedangsari Gunung Kidul Yogyakarta aimed to determine the implementation of ‘teaching factory’ in Boutiqe Fashion...
Global Distribution and Characteristics of Research Facilities Participating in Phase III Oncology Trials
Global Distribution and Characteristics of Research Facilities Participating in Phase III Oncology Trials
ABSTRACT
Background
Research infra-structure is essential for conducting phase III cancer clinical trials as its lack precludes...
Mécanismes et verrous de la carbonatation minérale du CO2 en voie aqueuse
Mécanismes et verrous de la carbonatation minérale du CO2 en voie aqueuse
La carbonatation minérale est une technique alternative de capture et stockage du CO2 anthropique. L'abondance des matériaux carbonatables sur terre en fait une solution à fort pot...
Thermodynamics and Industrial Trial on Increasing the Carbon Content at the BOF Endpoint to Produce Ultra-Low Carbon IF Steel by BOF-RH-CSP Process
Thermodynamics and Industrial Trial on Increasing the Carbon Content at the BOF Endpoint to Produce Ultra-Low Carbon IF Steel by BOF-RH-CSP Process
Abstract
Thermodynamic analysis was performed to obtain the relation between the carbon content at the BOF endpoint and the dissolved oxygen ...
Etude cinétique expérimentale et modélisation de la réaction de carbonatation de l'oxyde de calcium.
Etude cinétique expérimentale et modélisation de la réaction de carbonatation de l'oxyde de calcium.
Les émissions anthropiques de dioxyde de carbone, gaz à effet de serre, sont considérées comme les principales causes du réchauffement climatique. Le captage du dioxyde de carbone ...
Evaluation of 3 Assays for Failure of Passive Transfer in Calves
Evaluation of 3 Assays for Failure of Passive Transfer in Calves
Abstarct
This study examined the sensitivity, specificity, predictive values, and classification accuracy of 3 commonly used screening tests for failure of passiv...
Patient-centered perspectives: Examining quality-of-life integration in phase III lung cancer trials (2019-2023).
Patient-centered perspectives: Examining quality-of-life integration in phase III lung cancer trials (2019-2023).
e23181 Background: In the dynamic landscape of lung cancer treatment, marked by precision medicine advancements, addressing the persistent global health challenge of lung cancer r...
Small Cell Lung Cancer and Tarlatamab: A Meta-Analysis of Clinical Trials
Small Cell Lung Cancer and Tarlatamab: A Meta-Analysis of Clinical Trials
Abstract
Introduction
Tarlatamab is a Delta-like ligand 3 (DLL3) -directed bispecific T-cell engager recently approved for use in patients with advanced small cell lung cancer (SCL...

