Steam-assisted biomass fractionation. I. Process considerations and economic evaluation

A series of process design and economics models have been created which calculate the process cost for several scenarios in steam-explosion/fractionation of wood. Steam-explosion/fractionation technology offers the opportunity to produce chemicals and materials from such biomass resources as wood processing residues, agricultural crop residues and waste paper. The models comprise a series of modular computer simulations, where each module summarizes a particular group of unit operations with respect to mass balance, energy requirements, and process cost including utilities, capital, labor, and other related costs. These modules are compiled into three groups of scenarios: (1) unprocessed steam-exploded biomass, (2) water extracted steam-exploded biomass, and (3) water and aqueous solvent (alkali or ethanol) extracted steam-exploded biomass. For the base case evaluated, the cost of producing a 50% moisture content (based on total weight) steam-exploded fiber amounts to the raw material cost plus $0.077 kg−1, dry basis. A water washed steam-exploded biomass fiber along with water-soluble solids (WSS) can be produced for $0.165 kg−1, plus raw material, if the WSS are recovered by evaporative concentration. A more delignified, steam-exploded fiber with recovery of WSS and an aqueous alkali soluble lignin can be produced for between $0.222 and $0.246 kg−1 of raw material processed, dry basis, depending on the lignin recovery option employed (i.e. evaporative concentration; precipitation from alkaline solution; or spray drying).

[1]  J. Lora,et al.  Autohydrolysis of aspen milled wood lignin , 1980 .

[2]  D. Gardner,et al.  Formulation of a lignin-based plywood adhesive from steam-exploded mixed harwood lignin , 1986 .

[3]  Gael D. Ulrich,et al.  A Guide to Chemical Engineering Process Design and Economics , 1984 .

[4]  C. Breuil,et al.  Assessment of pretreatment conditions to obtain fast complete hydrolysis on high substrate concentrations , 1989 .

[5]  J N Saddler,et al.  Steam‐explosion pretreatment of wood: Effect of chip size, acid, moisture content and pressure drop , 1986, Biotechnology and bioengineering.

[6]  J. Wright Ethanol from biomass by enzymatic hydrolysis , 1988 .

[7]  H. Grethlein,et al.  Pretreatment for enhanced hydrolysis of cellulosic biomass. , 1984, Biotechnology advances.

[8]  L. Lorenz,et al.  KINETIC MODELING OF HARDWOOD PREHYDROLYSIS. PART III. WATER AND DILUTE ACETIC ACID PREHYDROLYSIS OF SOUTHERN RED OAK , 1986 .

[9]  L. Viikari,et al.  Biotechnical utilization of wood carbohydrates after steaming pretreatment , 1985, Applied Microbiology and Biotechnology.

[10]  A. H. Conner Kinetic Modeling of Hardwood Prehydrolysis. Part I. Xylan Removal by Water Prehydrolysis , 1984 .

[11]  M. Vignon,et al.  Saccharification of steam‐exploded poplar wood , 1991, Biotechnology and bioengineering.

[12]  S. Parekh,et al.  SO2 prehydrolysis for high yield ethanol production from biomass , 1988 .

[13]  C. Biermann,et al.  Steam explosion of mixed hardwood chips as a biomass pretreatment , 1983 .

[14]  P. Schweitzer,et al.  Handbook of Separation Techniques for Chemical Engineers , 1997 .

[15]  K. Sarkanen,et al.  The chemistry of several novel bioconversion lignins , 1983 .

[16]  Robert H. Marchessault,et al.  Characterization of aspen exploded wood lignin , 1982 .

[17]  Jürgen Puls,et al.  Differences in Xylan Degradation by Various Noncellulolytic Thermophilic Anaerobes and Clostridium thermocellum , 1985, Applied and environmental microbiology.

[18]  C. Biermann,et al.  Steam explosion of mixed hardwood chips, rice hulls, corn stalks, and sugar cane bagasse , 1984 .

[19]  R. Dekker,et al.  Enzymic saccharification of sugarcane bagasse pretreated by autohydrolysis–steam explosion , 1983, Biotechnology and bioengineering.

[20]  T. Schultz,et al.  Comparison of the pretreatment of sweetgum and white Oak by the steam explosion and RASH Processes , 1989 .

[21]  M. Wayman,et al.  Hydrolysis of biomass by sulphur dioxide , 1984 .

[22]  R. Overend,et al.  Fractionation of lignocellulosics by steam-aqueous pretreatments , 1987, Philosophical Transactions of the Royal Society of London. Series A, Mathematical and Physical Sciences.

[23]  J. Puls,et al.  Potential of Steaming Hardwoods and Straw for Feed and Food Production , 1978 .

[24]  E. L. Springer,et al.  Kinetic modeling of hardwood prehydrolysis. Part II. Xylan removal by dilute hydrochloric acid prehydrolysis , 1985 .

[25]  Wil Lepkowski Bhopal Disaster Spotlights Chemical Hazard Issues: At Institute, W.Va., hearing, government and industry re-examine environmental concerns of communities near chemical plants , 1984 .

[26]  D. Feinberg,et al.  Value of furfural/ethanol coproduction from acid hydrolysis processes , 1983 .

[27]  Klaus D. Timmerhaus,et al.  Plant design and economics for chemical engineers , 1958 .

[28]  P. A. Rice,et al.  Economic contribution of lignins to ethanol production from biomass , 1985 .

[29]  J. Lora,et al.  Organosolv pulping: a versatile approach to wood refining , 1985 .

[30]  Ricardo San Martin,et al.  Steam hydrolysis of pine (Pinus radiata) sawdust , 1985 .