Process for production of sulphuric acid
US-8926936-B2 · Jan 6, 2015 · US
US10294105B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10294105-B2 |
| Application number | US-201615744307-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 30, 2016 |
| Priority date | Jul 27, 2015 |
| Publication date | May 21, 2019 |
| Grant date | May 21, 2019 |
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The above mentioned invention describes a process for cooling a gas mixture of SO 2 and/or SO 3 and water, wherein the gas mixture is cooled by means of a first heat exchanger carrying a coolant. The temperature of the coolant lies above the dew point of the gas or gas mixture.
Opening claim text (preview).
The invention claimed is: 1. A process for cooling a gas mixture of SO 2 and/or SO 3 and water comprising cooling the gas mixture with a first heat exchanger carrying a coolant, wherein the temperature of the coolant lies above the dew point of the gas or gas mixture, the coolant is water, and the dew point τ given in ° C. is calculated according to the following equation: τ = e ( 6.0006 - ( 3.158 · 10 - 7 p · 1.244 · 10 - 9 · c ) ) + ( 0.1387 · ln ( p · 1.244 · 10 - 9 · c ) ) with p = gas pressure in mbar a and c = water content in mg / Nm 3 . 2. The process according to claim 1 , wherein the water content is determined by a method based on a laser diode system. 3. The process according to claim 1 , wherein the gas mixture is cooled from a temperature between 400 and 500° C. to a temperature between 130 and 180° C. 4. The process according to claim 1 , wherein the coolant is heated so that the coolant at least partly evaporates. 5. The process according to claim 1 , wherein the gas mixture is guided through the first heat exchanger counterflow to the coolant. 6. The process according to claim 1 , wherein a second heat exchanger is provided before the first heat exchanger and that the coolant is guided first through the second heat exchanger and then through the first heat exchanger. 7. An apparatus for cooling a gas mixture of SO 2 and/or SO 3 and water comprising a first coolant-carrying heat exchanger with an inlet and an outlet for the coolant, a control or regulating device which adjusts the temperature of the coolant at the inlet to a temperature above the dew point of the gas or gas mixture, and a measuring device for determining the water content of the gas mixture, which is coupled with the control or regulating device such that the dew point τ given in ° C. is calculated according to the following equation: τ = e ( 6.0006 - ( 3.158 · 10 - 7 p · 1.244 · 10
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