Gas conditioning process and system for extracting a condensable vapour from a supplied gas
A process for extracting a condensable vapor from a supplied gas, comprising the steps of: i) condensing the condensable vapor by cooling the supplied gas at a condensing surface, such that the supplied gas is divided into at least one condensed fraction and a product gas; while ii) removing the at least one condensed fraction from the condensing surface by mechanical scraping means.
1. A process for extracting a condensable vapour from a supplied gas, comprising the steps of:
i) cooling the supplied gas at a first condensing surface; wherein said first condensing surface is temperature controlled to a first temperature for condensing a portion of the condensable vapour in the supplied gas, such that the supplied gas is divided into a preliminary condensed fraction and a process gas; while removing the preliminary condensed fraction at the first condensing surface with mechanical scraping means; and
ii) cooling the process gas at a second condensing surface; Wherein at the second condensing surface is temperature controlled to a second temperature for condensing a further proportion of the remaining condensable vapour in the process gas, such that the process gas is divided into a subsequent condensed fraction and a product gas; while removing the subsequent condensed fraction at the condensing surface with mechanical scraping means;
wherein the preliminary condensed fraction has a higher dew point temperature than the subsequent condensed fraction; and wherein the preliminary condensed fraction has a higher viscosity than the subsequent condensed fraction at any given temperature below the second temperature, and wherein the process further comprises the steps of:
a) collecting the removed subsequent condensed fraction at a first location wherein said first location is temperature controlled to the second temperature; and
b) conveying the subsequent condensed fraction mechanically from the first location to a second location; wherein said second location is temperature controlled to the first temperature for heating and/or vaporizing said subsequent condensed fraction to form a heated subsequent fraction; and
c) collecting the removed preliminary condensed fraction at the second location; and
d) conveying the preliminary condensed fraction and heated subsequent fraction mechanically from the second location to a third location; wherein said third location is temperature controlled to a temperature higher than the first temperature for heating and/or vaporizing said heated subsequent fraction and preliminary condensed fraction to form a concentrated condensable vapour; and
e) extracting the concentrated condensable vapour from the third location.
2. The process as claimed in claim 1 , wherein the supplied gas is a product of coal gasification or pyrolysis of a carbonaceous feed; and wherein the condensable vapor comprises hydrocarbon which has a nongaseous phase at a standard ambient temperature of 25° C. and pressure of 1 atm.
3. The process as claimed in claim 2 , wherein the supplied gas comprises methane; and wherein the condensable vapor comprises tars.
4. The process as claimed in claim 1 , further comprising a step of controlling supplied gas temperature with a supplied gas heat exchanger prior to the step of cooling the supplied gas; wherein the supplied gas prior to the cooling step is substantially free from the at least one condensed fraction.
5. The process as claimed in claim 1 , further comprising a step of filtering supplied gas with a filter prior to the step of cooling said supplied gas.
6. The process as claimed in claim 1 , further comprising a step of scrubbing the product gas with a scrubber; wherein the scrubbed product gas is subsequently dried using a gas dryer.
7. The process as claimed in claim 1 , wherein step ii) is repeated at further condensing surfaces using the product gas of the previous step as an input gas, and steps c)-d) are repeated at further locations using a condensed fraction a further condensing surfaces and/or the heated condensed fraction of the previous step as input material.
8. A gas conditioning system for carrying out the process as claimed in claim 1 , comprising at least one condensing unit, wherein a thermally controlled conveying means is provided for heating and/or vaporizing the preliminary condensed fraction and subsequent condensed fraction removed from the at least one condensing unit to form the concentrated condensable vapour; wherein the thermally controlled conveying means is a heating extruder or a heating scraped surface heat exchanger; wherein the condensing unit comprises the first condensing surface, mechanical scraping means for removing condensed fractions from the first condensing surface, the second condensing surface, and mechanical scraping means for removing condensed fractions from the second condensing surface; wherein each of the first condensing surface and the second condensing surface are individually temperature controlled; wherein the thermally controlled conveying means comprises the first location, second location and third location for heating and vaporising the condensed fraction removed from the at least one condensing unit; where the first location, second location and third location are sequentially connected; and wherein the temperature increases progressively from the first location to the third location.
9. The gas conditioning system as claimed in claim 8 comprising at least two condensing units; wherein the at least two condensing units comprise a first condensing unit as the first condensing surface and a second condensing unit as the second condensing surface.
10. The gas conditioning system as claimed in claim 9 , wherein the at least two condensing units are serially connected; and wherein each of the at least two condensing units are individually temperature controlled.
11. The gas conditioning system as claimed in claim 8 , wherein the condensing unit is an extruder comprising mechanical scraping means for conveying and removing the preliminary condensed fraction and subsequent condensed fraction from the condensing surface.
12. The gas conditioning system as claimed in claim 11 , wherein the mechanical scraping means is helical screws; wherein said extruder comprises heating/cooling jackets to provide temperature control.
13. The gas conditioning system as claimed in claim 12 , wherein the helical screws comprising a nonstick coating for efficient discharge of the preliminary condensed fraction and subsequent condensed fraction from the helical screws.
14. The gas conditioning system as claimed in claim 8 , wherein the condensing unit is a scraped surface heat exchanger comprising mechanical scraping means for conveying and removing the preliminary condensed fraction and subsequent condensed fraction from the condensing surface.
15. The gas conditioning system as claimed in claim 14 , wherein the mechanical scraping means comprises one or more piston or scraper; wherein the scraped surface heat exchanger comprises a barrel enclosed in a heating/cooling jackets to provide temperature control.
16. The gas conditioning system as claimed in claim 15 , wherein the contacting surfaces between the one or more piston or scraper and the barrel comprising a hard-wearing coating for protecting said contacting surface.
17. The gas conditioning system as claimed in claim 16 , wherein the hard-wearing coating is boron-nitride.
18. The gas conditioning system as claimed in claim 8 , wherein the condensing unit comprises gas/liquid separation means for separating any condensed fraction from gas.
19. A process for extracting a condensable vapour from a supplied gas, comprising the steps of:
i) cooling the supplied gas at a first condensing surface; wherein said first condensing surface is temperature controlled to a first temperature for condensing a portion of the condensable vapour in the supplied gas, such that the supplied gas is divided into a preliminary condensed fraction and a process gas; while removing the preliminary condensed fraction at the first condensing surface with mechanical scraping means; and
ii) cooling the process gas at a second condensing surface; wherein at the second condensing surface is temperature controlled to a second temperature for condensing a further proportion of the remaining condensable vapour in the process gas, such that the process gas is divided into a subsequent condensed fraction and a product gas; while removing the subsequent condensed fraction at the condensing surface with mechanical scraping means;
wherein the preliminary condensed fraction has a higher dew point temperature than the subsequent condensed fraction; and wherein the preliminary condensed fraction has a higher viscosity than the subsequent condensed fraction at any given temperature below the second temperature, and wherein the process further comprises the steps of:
a) collecting the removed subsequent condensed fraction at a first location wherein said first location is temperature controlled to at least the
second temperature; and b) collecting the removed preliminary condensed fraction at the second location; wherein said second location is temperature controlled to at least the first temperature.
20. The process as claimed in claim 19 , wherein the supplied gas is a product of coal gasification or pyrolysis of a carbonaceous feed; and wherein the condensable vapor comprises hydrocarbon which has a non-gaseous phase at a standard ambient temperature of 25° C. and pressure of 1 atm.
21. The process as claimed in claim 20 , wherein the supplied gas comprises methane; and wherein the condensable vapor comprises tars.
22. The process as claimed in claim 19 , further comprising a step of filtering supplied gas with a filter prior to the step of cooling said supplied gas.
23. The process as claimed in claim 19 , wherein step ii) is repeated at further condensing surfaces using the product gas of the previous step as an input gas, and step b) is repeated at further locations using fractions condensed at the further condensing surfaces as input material.
24. A gas conditioning system for carrying out the process as claimed in claim 19 , comprising at least one condensing unit, a first location, and a second location; wherein the condensing unit comprises the first condensing surface, mechanical scraping means for removing condensed fractions from the first condensing surface, the second condensing surface, and mechanical scraping means for removing condensed fractions from the second condensing surface; wherein each of the first condensing surface and the second condensing surface are individually temperature controlled; wherein the first location is adapted to receive condensed fractions from the second condensing surface and temperature controlled to the same temperature as the second condensing surface or higher; wherein the second location is adapted to receive condensed fractions from the first condensing surface and temperature controlled to the same temperature as the first condensing surface or higher.
25. The gas conditioning system as claimed in claim 24 comprising at least two condensing units; wherein the at least two condensing units comprise a first condensing unit as the first condensing surface and a second condensing unit as the second condensing surface.
26. The gas conditioning system as claimed in claim 25 , wherein the at least two condensing units are serially connected; and wherein each of the at least two condensing units are individually temperature controlled.
27. The gas conditioning system as claimed in claim 24 , wherein the condensing unit is a scraped surface heat exchanger comprising mechanical scraping means for conveying and removing the preliminary condensed fraction and subsequent condensed fraction from the condensing surface.
28. The gas conditioning system as claimed in claim 27 , wherein the mechanical scraping means comprises one or more piston or scraper; wherein the scraped surface heat exchanger comprises a barrel enclosed in a heating/cooling jackets to provide temperature control.