It's a bit difficult to say that acid/base catalysis "falls
down," whether it be the ambient procedure as presented by Aleks
Kac or a HTP industrial procedure.

Most of what industry achieves under high pressure and
temperature can be achieved at STP by conducting the reaction
over prolonged periods, at moderate temperature and in several
stages when necessary.

To date we have experienced repeated success with STP
esterification, simply by prolonging the esterification period to
36-48 hours, generating a complete transesterification reaction
on 3.5% FFA feedstock with but 1.5 grams of KOH per liter of oil
over a 36 hour period.

Whether a repeat cycle is used on the esterification side or not,
it is necessary to separate the feedstock from any layers that
formed during the esterification prior to conducting the repeat
cycle or the base stage.

Todd Swearingen

----- Original Message -----
From: goat industries <[EMAIL PROTECTED]>
To: <biofuels-biz@yahoogroups.com>
Sent: Monday, August 19, 2002 4:19 PM
Subject: [biofuels-biz] hi ffa feed stocks


> Check out work done by Canakci and Van Gerpen. I'm trying out
their ideas,
> but finding it difficult to get good results. Also, an acid
value of 1mg
> KOH/g = 0.5 % FFA. They identiified water formation in the acid
stage as the
> inhibiting part of the reaction, which is where Alek's
'foolproof' method
> falls down (apparently).
>
>
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