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Recovery of volatile products from fermentation broth

A technology for fermentation liquid and fermenter, which is applied in the directions of liquid production bioreactor, fermentation, gas production bioreactor, etc., can solve problems such as reducing the fouling rate

Inactive Publication Date: 2009-10-21
DOW GLOBAL TECH LLC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Although by adding CO 2 The fouling rate can be reduced by injecting bubbles of gas or other gases into the fermenter vessel near the surface outside the membrane (fermenter side) to wash the outside of the membrane, or by injecting liquid flow into the membrane surface as in cross-flow membrane modules, but Fouling rate is often a significant issue at high cell concentrations in culture medium

Method used

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  • Recovery of volatile products from fermentation broth
  • Recovery of volatile products from fermentation broth
  • Recovery of volatile products from fermentation broth

Examples

Experimental program
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Embodiment 1

[0150] Using Aspen Plus from AspenTech Engineering Suite 12.1 (program) TM (Trademark of AspenTech) software calculates process performance and determines preferred operating conditions and design specifications for a standard fermentor unit 200 (not shown) + stirred VSS unit 10 . The Aspen flow chart is shown in image 3 middle. Aspen Plus TM Simulations were constructed to utilize the validated Vapor-Liquid Equilibrium (VLE) and Liquid-Liquid Equilibrium (LLE) models. VLE and LLE models include acetone, butanol, ethanol, and water, as well as noble gases. The simulation results are summarized in Table 1. For these calculations, the ABE fermentation was assumed to have a productivity of typically 1.5 g of 1-butanol produced per liter of fermentor vessel volume per hour. Given that the VSS unit 10 can be operated at 200 mm Hg without damaging the cells, the preferred operating and design conditions and resulting performance are highlighted. The actual pressure limit can ...

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Abstract

Provided are apparatuses and processes for the removal and purification of fermentation prepared one or more volatile organic compounds. The apparatuses comprise a fermentor unit, a vacuum side stripper unit (10), and, optionally, one or more of a pressure-swing adsorption unit, a dual-function column, a dividing wall distillation column unit, and a means for inducing phase separation of a mixture of a volatile organic compound and water.

Description

technical field [0001] The present invention relates to apparatus and methods for producing volatile organic compounds (VOCs) by fermentation of a fermentation broth and for removing VOCs from the fermentation broth. Background technique [0002] Butanol is an important industrial chemical that is used, for example, as a fuel, a fuel additive, or as a precursor or intermediate in the production of other useful chemicals. [0003] In recent years, the cost of butanol production by hydroformylation technology has increased significantly due to the high cost of propylene feedstock. Production of butanol by fermentation represents an alternative process technology that offers the potential for low-cost production utilizing lower-cost feedstocks. [0004] In the production of butanol or other solvents or volatile organic compounds, an important aspect of the fermentation process is the purification of said compounds. Another important aspect is the control and removal of solven...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D3/00B01D3/30B01D3/10
CPCY02E50/17C12M29/02C12M21/04C12M21/12C12M47/10B01D3/343C12P7/16C12M27/20Y02E50/10
Inventor 蒂莫西·C·弗兰克杰夫·A·费里奥保罗·E·斯万森于尔根·吕斯克
Owner DOW GLOBAL TECH LLC