Reaction of Hydrogen Chloride Gas with Sodium Carbonate and Its Deep Removal in a Fixed-Bed Reactor

2014 ◽  
Vol 53 (49) ◽  
pp. 19145-19158 ◽  
Author(s):  
Miloslav Hartman ◽  
Karel Svoboda ◽  
Michael Pohořelý ◽  
Michal Šyc ◽  
Siarhei Skoblia ◽  
...  
Keyword(s):  
Hydrogen Chloride ◽  
Sodium Carbonate ◽  
Fixed Bed ◽  
Fixed Bed Reactor

Reactivity of the solid sodium carbonate towards the gaseous hydrogen chloride and the sulphur dioxide

1983 ◽  
Vol 48 (12) ◽  
pp. 3500-3507 ◽  
Author(s):  
Karel Mocek ◽  
Erich Lippert ◽  
Emerich Erdös
Keyword(s):  
Hydrogen Chloride ◽  
Sodium Carbonate ◽  
Sulphur Dioxide ◽  
Active Form ◽  
Fixed Bed ◽  
Fixed Bed Reactor ◽  
Anhydrous Sodium Carbonate ◽  
A Value ◽  
Partial Pressures ◽  
Inactive Form

The rate of reaction of the anhydrous sodium carbonate with the hydrogen chloride and its mixture with sulphur dioxide was measured in an integral fixed-bed reactor. Reactivity of the active sodium carbonate towards the hydrogen chloride is lower as compared with its reactivity towards the sulphur dioxide. A relationship was found between the reactivity of the solid and the way of its preparation. The inactive form of the sodium carbonate is inactive towards both the sulphur dioxide and the hydrogen chloride. The active form of the sodium carbonate exhibits towards the hydrogen chloride a reactivity which is by orders of magnitude higher than that of the inactive form. The variation of the ratio of partial pressures of the hydrogen chloride and the sulphur dioxide in the reaction with the sodium carbonate does not affect significantly the total degree of the solid conversion, which attained a value of 65% in laboratory experiments. The degree of gas purification from the acid components did not fall under a value of 99% up to a solid conversion of about 50% at a mean gas contact time of about 10-2 s.

The Adsorption and Desorption Breakthrough Behavior of Hydrogen Chloride Gas Mixture on Zeolite 13X Pellet in a Fixed Bed Reactor

2015 ◽  
Vol 48 (3) ◽  
pp. 202-211 ◽  
Author(s):  
Jae-Young Kim ◽  
Dae-Hyun Kyung ◽  
Young Cheol Park ◽  
Sung-Ho Jo ◽  
Ho-Jung Ryu ◽  
...  
Keyword(s):  
Hydrogen Chloride ◽  
Fixed Bed ◽  
Fixed Bed Reactor ◽  
Gas Mixture ◽  
Adsorption And Desorption ◽  
Zeolite 13X

Synthesis and Modification of Zeolite ZSM-5 Catalyst with Solutions of Calcium Carbonate (CaCO3) and Sodium Carbonate (Na2CO3) for Methanol to Gasoline Conversion

2018 ◽  
Vol 16 (7) ◽  
Author(s):  
Ehsan Kianfar ◽  
Mahmoud Salimi ◽  
Vahid Pirouzfar ◽  
Behnam Koohestani
Keyword(s):  
Calcium Carbonate ◽  
Sodium Carbonate ◽  
Catalyst Activity ◽  
Fixed Bed ◽  
Fixed Bed Reactor ◽  
Base Catalyst ◽  
Structure And Morphology ◽  
Methanol To Gasoline ◽  
Molar Solution ◽  
Ft Ir

Abstract In this article, the ZSM-5 catalyst was used as the base catalyst and its structure was modified for conducting Methanol to Gasoline reactions. ZSM-5 catalyst reacts to the solutions with diverse concentrations of calcium carbonate (CaCO3) and sodium carbonate (Na2CO3), and consequently, some changes were applied to its internal structure. Thus, Methanol to Gasoline (MTG) process was carried out under pressure of 1 atm, the temperature of 400°C, and specific surface area of 300 m2g-1 on synthetic zeolite ZSM-5 catalyst by a fixed-bed reactor. Structure and morphology of the synthesized catalyst were investigated by XRD, FT-IR, SEM, XRF and BET analyses. The effect of CaCO3 and Na2CO3 solutions used for catalyst modification on the distribution of hydrocarbon products were studied and compared to ZSM-5 catalyst. The result of catalyst activity evaluation tests shows that the modified catalyst with a 0.1 molar solution of CaCO3 and Na2CO3 provides the highest selectivity and efficiency compared to the hydrocarbons in boiling point range of C6+ gasoline.

Recovery of Chlorine from Anhydrous Hydrogen Chloride

2008 ◽  
Vol 6 (1) ◽  
Author(s):  
Usha Virendra Reddy ◽  
Vijaya Lakshmi Cheedipudi ◽  
Satyavathi Bankupalli ◽  
Viswanath Kotra
Keyword(s):  
Hydrogen Chloride ◽  
Waste Disposal ◽  
Copper Chloride ◽  
Fixed Bed ◽  
Raw Material ◽  
Toxic Waste ◽  
Fixed Bed Reactor ◽  
Stable Operation ◽  
Titanium Chloride ◽  
Disposal Problem

Chlorine and hydrogen chloride are classified as potentially hazardous and toxic chemicals. Large-scale industrial processes worldwide use chlorine as primary raw material from which hydrogen chloride is obtained as a major byproduct. Hydrogen chloride is sold as aqueous HCl or used as a raw material for the production of chlorinated products, but the quantity of HCl produced by chlorine processes is much more than what the market can absorb, resulting in a toxic waste disposal problem. Recovery of material chlorine from this hydrogen chloride is very important and is of utmost industrial interest as it would cut down on the production of chlorine at the same time solve the waste disposal problem. It is theoretically possible to convert hydrogen chloride to chlorine for the recycling and reuse of chlorine. In this paper we have developed a process for recovery of chlorine from anhydrous hydrogen chloride obtained as a byproduct during low temperature vapor phase hydrolysis of titanium chloride to get TiO2. It is a two-stage process where chlorination is carried out in a fixed bed reactor using copper oxide catalyst at a temperature in the range of 423-523 K followed by oxidation of copper chloride catalyst in a second fixed bed reactor operating at 573-653 K. This process operates under conditions in which the catalyst does not volatilize and in which the activity of the catalyst remains stable. Operation at relatively moderate temperature prevents corrosion and minimizes the extrinsic energy input required. The chlorine recovery process makes the new generation chloride process for synthesis of TiO2 economical.

Contribution to the study of the reaction between solid sodium carbonate and gaseous sulphur dioxide

1981 ◽  
Vol 46 (10) ◽  
pp. 2281-2288 ◽  
Author(s):  
Jiří Vobiš ◽  
Karel Mocek ◽  
Emerich Erdös
Keyword(s):  
Water Vapour ◽  
Rate Constant ◽  
Sodium Carbonate ◽  
Sulphur Dioxide ◽  
Heterogeneous Reaction ◽  
Fixed Bed ◽  
Effective Rate Constant ◽  
Fixed Bed Reactor ◽  
True Rate ◽  
Partial Pressures

The heterogeneous reaction between solid sodium carbonate and gaseous sulphur dioxide of partial pressures from 1.2 to 7.5 kPa has been investigated in a fixed-bed reactor at temperatures of 54 and 81 °C in the presence of water vapour of partial pressures from 0.30 to 1.25 kPa. An independence of the reaction course of the sulphur dioxide content in the gas phase and a linear dependence of the reaction rate on the partial pressure of water vapour were found under the above conditions. The rate equation derived previously has been simplified and the set of differential equations describing the reaction in a fixed bed has been solved. The relations obtained have been applied to an evaluation of the effective rate constant. The true rate constant has been estimated to be independent of temperature.

Reaction of Solid Sorbents with Hydrogen Chloride Gas at High Temperature in a Fixed-Bed Reactor

2005 ◽  
Vol 19 (6) ◽  
pp. 2229-2234 ◽  
Author(s):  
Binlin Dou ◽  
Bingbing Chen ◽  
Jinsheng Gao ◽  
Xingzhong Sha
Keyword(s):  
High Temperature ◽  
Hydrogen Chloride ◽  
Fixed Bed ◽  
Fixed Bed Reactor ◽  
Solid Sorbents
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