System and method for purification of gasses such as fuel gasses
AssigneesDanmarks Tekniske Universitet, Elplatek A/S
InventorsSebastian Nis Bay Villadsen, Philip Loldrup Fosbøl, Jan Boye Rasmussen
Life of this patent
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Abstract
The present disclosure provides a system and a method for cleaning of gas.
Claims65
A system for cleaning of gas, said system comprising:
- i. an electrolysis element comprising separate anolyte- and catholyte compartments for generation of an anolyte and a catholyte, respectively, and
- ii. a wet scrubbing element comprising:
- a gas inlet and a gas outlet defining the direction of the gas flow;
- an anolyte inlet and a catholyte inlet, wherein the catholyte inlet is separate and downstream from the anolyte inlet relative to the direction of the gas flow;
- and
- one or more scrubbing liquid outlets
- said one or more scrubbing liquid outlets being configured to at least in part supply the electrolysis element.
The system according to any one of the preceding claims, wherein the electrolysis element bypass is configured to transfer liquid from the scrubbing liquid outlets to the anolyte inlet and/or the catholyte inlet by bypassing the electrolysis element.
The system according to any one of the preceding claims, further comprising:
- i. a liquid transferring element from the anolyte compartment to the anolyte inlet,
- ii. a liquid transferring element from the catholyte compartment to the catholyte inlet, and/or
- iii. one liquid transferring element from each of the one or more scrubbing liquid outlets to the electrolysis element.
The system according to any one of the preceding claims, further comprising:
- i. a liquid transferring element from the anolyte compartment to the anolyte inlet,
- ii. a liquid transferring element from the catholyte compartment to the catholyte inlet, and
- iii. one or more liquid transferring elements from the one or more scrubbing liquid outlets to the electrolysis element.
The system according to any one of the preceding claims, comprising two wet scrubbing elements connected in series with respect to the gas flow.
The system according to any one of the preceding claims, wherein the cleaning of gas is desulfurisation of gas.
The system according to any one of the preceding claims, said system being configured to desulfurise gas.
The system according to any one of the preceding claims, wherein the desulfurisation of gas is the full or partial removal of one or more sulfur compounds from the gas.
The system according to any one of the preceding claims, wherein the system is configured to full or partial removal of one or more sulfur compounds from the gas.
The system according to any one of the preceding claims, wherein the desulfurisation of gas is the reduction of H2S content in the gas.
The system according to any one of the preceding claims, wherein the gas is a fuel gas, such as coke-oven gas, natural gas, gas from geothermal plants, shale gas, or landfill gas.
The system according to any one of the preceding claims, wherein the gas is selected from the group consisting of process gas from the production of bio-technical products and exhaust gas from chemical factories.
The system according to any one of the preceding claims, wherein the electrolysis element comprises a single liquid inlet supplying both the anolyte compartment and the catholyte compartment.
The system according to any one of the preceding claims, wherein the electrolysis element comprises a single liquid inlet configured to supply both the anolyte compartment and the catholyte compartment.
The system according to any one of the preceding claims, wherein the electrolysis element comprises one liquid inlet supplying the anolyte compartment and another liquid inlet supplying the catholyte compartment.
The system according to any one of the preceding claims, wherein the electrolysis element comprises one liquid inlet configured to supply the anolyte compartment and another liquid inlet supplying the catholyte compartment.
The system according to any one of the preceding claims, wherein the one or more wet scrubbing elements are one or more wet scrubbing towers.
The system according to any one of the preceding claims, comprising a wet scrubbing element having a scrubbing liquid outlet, wherein said scrubbing liquid outlet is positioned between the anolyte inlet and the catholyte inlet.
The system according to any one of the preceding claims, wherein the scrubbing liquid outlet supply the wet scrubbing element at the anolyte inlet.
The system according to any one of the preceding claims, wherein the scrubbing liquid outlet is configured to supply the wet scrubbing element at the anolyte inlet.
The system according to any one of the preceding claims, wherein the scrubbing liquid outlet supply the wet scrubbing element at the catholyte inlet.
The system according to any one of the preceding claims, wherein the scrubbing liquid outlet is configured to supply the wet scrubbing element at the catholyte inlet.
The system according to any one of the preceding claims, wherein the scrubbing liquid outlet supply both the electrolysis element and the wet scrubbing element at the anolyte inlet.
The system according to any one of the preceding claims, wherein the scrubbing liquid outlet is configured to supply both the electrolysis element and the wet scrubbing element at the anolyte inlet.
The system according to any one of the preceding claims, wherein the scrubbing liquid outlet supply both the electrolysis element and the wet scrubbing element at the catholyte inlet.
The system according to any one of the preceding claims, wherein the scrubbing liquid outlet is configured to supply both the electrolysis element and the wet scrubbing element at the catholyte inlet.
The system according to any one of the preceding claims, wherein part of the catholyte, but not all of the catholyte, is being introduced to the wet scrubbing element at the anolyte inlet.
The system according to any one of the preceding claims, wherein the system is configured to introduce part, but not all of the catholyte, to the wet scrubbing element at the anolyte inlet.
The system according to any one of the preceding claims, wherein:
- i. the system comprises a first wet scrubbing element and a second wet scrubbing element,
- ii. the anolyte compartment supplies a first wet scrubbing element at its anolyte inlet,
- iii. the catholyte compartment supplies a second wet scrubbing element at its catholyte inlet,
- iv. the liquid outlet of the first wet scrubbing element supplies the electrolysis element and the anolyte inlet of the first wet scrubbing element, and
- v. the liquid outlet of the second wet scrubbing element supplies the electrolysis element and the catholyte inlet of the second wet scrubbing element.
The system according to any one of the preceding claims, wherein:
- i. the system comprises a first wet scrubbing element and a second wet scrubbing element,
- ii. the anolyte compartment is configured to supply a first wet scrubbing element at its anolyte inlet,
- iii. the catholyte compartment is configured to supply a second wet scrubbing element at its catholyte inlet,
- iv. the liquid outlet of the first wet scrubbing element is configured to supply the electrolysis element and the anolyte inlet of the first wet scrubbing element, and
- v. the liquid outlet of the second wet scrubbing element is configured to supply the electrolysis element and the catholyte inlet of the second wet scrubbing element.
The system according to any one of the preceding claims, wherein the one or more wet scrubbing elements are two wet scrubbing towers.
The system according to any one of the preceding claims, wherein the one or more wet scrubbing elements is a single wet scrubbing tower.
The system according to any one of the preceding claims comprising a single wet scrubbing tower, wherein the catholyte inlet is positioned downstream of the anolyte inlet relative to the direction of the gas flow.
The system according to any one of the preceding claims, wherein the single scrubbing tower comprises a single scrubbing liquid outlet upstream of the anolyte inlet.
The system according to any one of the preceding claims, wherein the single scrubbing tower comprises a scrubbing liquid outlet between the catholyte inlet and the anolyte inlet, and a further scrubbing liquid outlet upstream of the anolyte inlet.
The system according to any one of the preceding claims comprising a first wet scrubbing element and a second wet scrubbing element, and wherein the direction of the gas flow is from the first wet scrubbing element to the second wet scrubbing element.
The system according to any one of the preceding claims, wherein the electrolysis element consumes 4.0 to 9.0 A per g H2S in the gas per hour, such as 5.0 to 7.4 A per g sulfur per hour, such as 5.2 to 7.2 A per g sulfur per hour, such as 5.4 to 7.0 A per g sulfur per hour, such as 5.6 to 6.8 A per g sulfur per hour, such as 5.8 to 6.6 A per g sulfur per hour, such as 6.0 to 6.4 A per g sulfur per hour, such as about 6.2 or 6.3 A per g sulfur per hour.
The system according to any one of the preceding claims, wherein the electrolysis element is configured to consume 4.0 to 9.0 A per g H2S in the gas per hour, such as 5.0 to 7.4 A per g sulfur per hour, such as 5.2 to 7.2 A per g sulfur per hour, such as 5.4 to 7.0 A per g sulfur per hour, such as 5.6 to 6.8 A per g sulfur per hour, such as 5.8 to 6.6 A per g sulfur per hour, such as 6.0 to 6.4 A per g sulfur per hour, such as about 6.2 or 6.3 A per g sulfur per hour.
The system according to any one of the preceding claims, wherein the electrolysis element is an electrochemical cell.
The system according to any one of the preceding claims further comprising one or more filters.
The system according to any one of the preceding claims, wherein the filter is positioned after the liquid outlet to a wet scrubbing element, such as after the wet scrubbing element to which the anolyte is supplied.
The system according to any one of the preceding claims, wherein the filter is positioned at or after the liquid outlet of the one or more wet scrubbing elements.
The system according to any one of the preceding claims, further comprising one or more pumps, such as:
- i. a pump prior to the electrolysis element,
- ii. a pump after the liquid outlet of one wet scrubbing element,
- iii. a pump prior to the anolyte inlet,
- iv. a pump prior to the catholyte inlet,
- v. a pump prior to the gas inlet,
- vi. a pump after the electrolysis element.
The system according to any one of the preceding claims, further comprising one or more filters, such as
- i. a filter prior to the electrolysis element,
- ii. a filter after the liquid outlet of one wet scrubbing element,
- iii. a filter prior to a pump,
- iv. a filter prior to the anolyte inlet,
- v. a filter prior to the catholyte inlet, and/or
- vi. a filter after the electrolysis element.
The system according to any one of the preceding claims, wherein the filter is a membrane filter or an ion chromatograph.
A fuel gas processing plant comprising the system according to any one of the preceding claims.
A method for desulfurisation of gas, said method comprising the steps of:
- i. providing an electrolysis element comprising separate compartments for generation of an anolyte and a catholyte,
- ii. providing one or more wet scrubbing elements,
- iii. providing a scrubbing liquid comprising an alkali chloride,
- iv. providing a gas comprising a sulfur compounds,
- v. conducting a electrochemical conversion of said scrubbing liquid to produce a anolyte comprising an oxidising agent and a catholyte comprising a base,
- vi. conducting a first scrubbing of said gas by contacting said gas with said anolyte in one wet scrubbing element, thereby obtaining a desulfurised gas and a spent scrubbing liquid, and conducting a second scrubbing of said gas by contacting said gas with said catholyte, thereby obtaining a desulfurised and dechlorinated gas and a spent scrubbing liquid, wherein the second scrubbing is conducted downstream of the first scrubbing relative to the direction of the gas flow.
- vii. recycling the spent scrubbing liquid by
- a. supplying at least parts of the spent scrubbing liquid to the electrolysis element.
The method according to any one of the preceding claims, wherein the sulfur compound is H2S.
The method according to any one of the preceding claims, wherein the content of H2S in the gas comprising the sulfur compound is 10 to 20000 ppm, such as 10 to 5000 ppm, such as 100 to 4000 ppm, such as 500 to 2500 ppm.
The method according to any one of the preceding claims, wherein the content of H2S in the gas comprising the sulfur compound varies substantially depending on feedstock composition and/or other external parameters such as temperature.
The method according to any one of the preceding claims, wherein said variation in H2S content is of a type such that a method comprising no introduction of catholyte would be insufficient to ensure removal of H2S without introducing Cl2 to the gas.
The method according to any one of the preceding claims, wherein said variation in H2S content is of a type such that a method comprising no introduction of catholyte would be insufficient to ensure removal of H2S without introducing Cl2 to the gas unless the current applied to the electrolysis element was continuously to accommodate the varying content of H2S.
The method according to any one of the preceding claims, wherein the method can tolerate a 100% variation in the content of H2S in the gas comprising sulfur compounds while still removing substantially all H2S from the gas and without introducing substantially any Cl2 to the gas.
The method according to any one of the preceding claims, wherein the method can tolerate a 100% variation in the content of H2S in the gas comprising sulfur compounds while still removing substantially all H2S from the gas and without introducing substantially any Cl2 to the gas, and without varying the current applied to the electrolysis element.
The method according to any one of the preceding claims, wherein no adjustment of the voltage and/or current supplied to electrolysis element is required to accommodate a 100% variation of H2S content in the gas.
The method according to any one of the preceding claims, wherein the alkali chloride is NaCl, KCl, and/or LiCl.
The method according to any one of the preceding claims, wherein the alkali chloride is NaCl.
The method according to any one of the preceding claims, wherein the scrubbing liquid comprises between 1 and 300 g/L NaCl, such as between 200 and 300 g/L NaCl, between 1 and 300 g/L KCl, such as between 200 and 300 g/L KCl, and/or between 1 and 300 g/L LiCl, such as between 200 and 300 g/L LiCl.
The method according to any one of the preceding claims, wherein the method does not comprise a step of adding NaOH, NaClO, HClO, or Cl2 to the scrubbing liquid.
A method of desulfurising a gas, said method comprising using the system according to any one of the preceding claims.
A system configured for performing the method according to any one of the preceding claims.
A gas desulfurised using the method according to any one of the preceding claims.
The gas according to any one of the preceding claims comprising:
- i. less than 100 ppm H2S, such as less than 75 ppm H2S, such as less than 50 ppm H2S, such as less than 25 ppm H2S, such as less than 20 ppm H2S, such as less than 15 ppm H2S, such as less than 10 ppm H2S, such as less than 5 ppm H2S, and
- ii. less than 100 ppm Cl2, such as less than 75 ppm Cl2, such as less than 50 ppm Cl2, such as less than 25 ppm Cl2, such as less than 20 ppm Cl2, such as less than 15 ppm Cl2, such as less than 10 ppm Cl2, such as less than 5 ppm Cl2.
Dependencies are inferred from the claim text.