Catalytic adsorbents obtained from municipal sludges, industrial sludges, compost and tobacco waste and a rotary drying process for their production
Abstract
A method for producing an adsorbent, having the steps of combining a first sludge and a second material to form a mixture, thermally drying the mixture, and pyrolizing the mixture using at least four temperature zones wherein each temperature zone is set between about 600° C. and 1,100° C. The first sludge is a municipal sludge or an industrial sludge, and the second material is a compost material or one of municipal sludge or industrial sludge differing from the first sludge. The compost material is at least one of tobacco waste, waste paper and wood char, or a combination thereof. Further, the drying can happen in two stages. Each stage can include two separate temperatures.
Claims
exact text as granted — not AI-modified1 . A method for producing an adsorbent, comprising the steps of:
combining a first sludge and a second material to form a mixture; thermally drying the mixture; and pyrolizing the mixture using at least four temperature zones wherein each temperature zone is set between about 600° C. and 1,100° C.
2 . The method of claim 1 , wherein the pyrolizing step further comprises the steps of:
setting a first temperature zone to about 600° C.; setting a second temperature zone to about 800° C.; setting a third temperature zone to about 900° C.; and setting a fourth temperature zone to about 1000° C.
3 . The method of claim 1 , wherein the drying step further comprises the steps of:
drying the mixture in a first temperature; and drying the mixture in a second temperature.
4 . The method of claim 3 , wherein the drying step further comprises the steps of:
setting the first temperature to about 385° C.; and setting the second temperature to about 230° C.
5 . The method of claim 1 , wherein the drying step further comprises the steps of:
drying the mixture in a first stage; and drying the mixture in a second stage.
6 . The method of claim 5 , wherein the drying step further comprises the steps of:
setting a first stage initial temperature; setting a first stage ending temperature; setting a second stage initial temperature; and setting a second stage ending temperature; wherein the first stage initial temperature is greater than the first stage ending temperature; and wherein the second stage initial temperature is greater than the second stage ending temperature.
7 . The method of claim 6 , wherein the first stage initial temperature is not equal to the second stage initial temperature; and
wherein the first stage ending temperature is not equal to the second stage ending temperature.
8 . The method of claim 7 , wherein the first stage initial temperature is about 370° C.;
wherein the first stage ending temperature is about 230° C.; wherein the second stage initial temperature is about 390° C.; and wherein the second stage ending temperature is about 200° C.
9 . The method of claim 1 wherein the first sludge is a municipal sludge or an industrial sludge, and
wherein the second material is a compost material or one of municipal sludge or industrial sludge differing from the first sludge.
10 . The method of claim 9 , wherein the compost material is at least one of tobacco waste, waste paper and wood char, or a combination thereof, and
wherein the first sludge is industrial sludge.
11 . The method of claim 9 , wherein the first sludge is industrial sludge, and
wherein the second material is municipal sludge.Join the waitlist — get patent alerts
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