Abstract: A fermentation unit and a method of carrying out fermentation are described. The fermentation unit can be transported from one facility to another to carry out a fermentation process. The fermentation unit and method allow for the fermentation of a C1-containing substrate from a source at a particular facility to produce products such as alcohols and acids. Examples of the source of the C1-containing substrate include without limitation steel manufacturing processes, coal and biomass gasification processes, coke manufacturing processes, etc. The fermentation unit can be housed within a container having a volume of less than about 6 m3.

Abstract: A fermentation unit and a method of carrying out fermentation are described. The fermentation unit can be transported from one facility to another to carry out a fermentation process. The fermentation unit and method allow for the fermentation of a C1-containing substrate from a source at a particular facility to produce products such as alcohols and acids. Examples of the source of the C1-containing substrate include without limitation steel manufacturing processes, coal and biomass gasification processes, coke manufacturing processes, etc. The fermentation unit can be housed within a container having a volume of less than about 6 m3.

Abstract: Apparatuses and associated methods are described for the efficient evaluation of C1-containing substrates, and especially for such evaluation conducted locally, or on-site, at a prospective facility for implementation of a biological conversion process for desired end product using a C1 carbon source. The exact composition of a given, industrial C1-containing substrate, as well as the range in composition fluctuations, are generally difficult to reproduce at a remote facility (e.g., a laboratory or a pilot-scale or demonstration-scale process), as required for the accurate prediction/modeling of commercial performance to justify large capital expenditures for commercial scale-up.

Abstract: Apparatuses and associated methods are described for the efficient evaluation of C1-containing substrates, and especially for such evaluation conducted locally, or on-site, at a prospective facility for implementation of a biological conversion process for desired end product using a C1 carbon source. The exact composition of a given, industrial C1-containing substrate, as well as the range in composition fluctuations, are generally difficult to reproduce at a remote facility (e.g., a laboratory or a pilot-scale or demonstration-scale process), as required for the accurate prediction/modeling of commercial performance to justify large capital expenditures for commercial scale-up.

Abstract: Apparatuses and associated methods are described for the efficient evaluation of C1-containing substrates, and especially for such evaluation conducted locally, or on-site, at a prospective facility for implementation of a biological conversion process for desired end product using a C1 carbon source. The exact composition of a given, industrial C1-containing substrate, as well as the range in composition fluctuations, are generally difficult to reproduce at a remote facility (e.g., a laboratory or a pilot-scale or demonstration-scale process), as required for the accurate prediction/modeling of commercial performance to justify large capital expenditures for commercial scale-up.

Abstract: Apparatuses and associated methods are described for the efficient evaluation of Cl-containing substrates, and especially for such evaluation conducted locally, or on-site, at a prospective facility for implementation of a biological conversion process for desired end product using a Cl carbon source. The exact composition of a given, industrial Cl-containing substrate, as well as the range in composition fluctuations, are generally difficult to reproduce at a remote facility (e.g., a laboratory or a pilot-scale or demonstration-scale process), as required for the accurate prediction/modeling of com?mercial performance to justify large capital expenditures for commercial scale-up.