The Pritchard Corporation

J. F. Pritchard and Company

Leonard K Swenson

John E Nobles

A method is disclosed of producing food grade carbon dioxide from an impure carbon dioxide source stream containing contaminants which may include light and heavy hydrocarbons (at least C.sub.1 to C.sub.3) and light sulfur compounds such as hydrogen sulfide and carbonyl sulfide as well as heavier sulfur constituents in the nature of mercaptans (RSH) and/or organic mono and disulfides (RSR and RSSR). Nitrogen, water and/or oxygen may also be present in varying amounts in the impure feed stream. The feed gas is first rectified with liquid carbon dioxide condensed from a part of the feed stream to remove heavy hydrocarbons and heavy sulfur compounds, then passed through an absorber to effect removal of the light sulfur compounds, next subjected to an oxidizing atmosphere capable of converting all of the C.sub.2 hydrocarbons and optionally a part of the methane to carbon oxides and water, chilled to condense the water in the remaining gas stream without formation of hydrates, liquefied for ease of handling and storage and finally stripped to remove residual contaminants such as methane, carbon monoxide and nitrogen to produce the final food grade carbon dioxide product.

Method and apparatus for producing food grade carbon dioxide

A fluid material is cooled through a temperature range exceeding 200.degree. F. by heat exchange with a single mixed refrigerant composition in a heat exchange zone forming a part of a closed loop refrigeration cycle thus assuring high reliability and low investment by virtue of simplification of the equipment required and ease of control thereof. The process is especially useful for liquefaction of natural gas. Refrigerant in the refrigeration loop containing constituents having increasingly lower boiling points is successively directed from a compression zone to a condensation zone, thence to a heat exchange zone, next expanded in an expansion zone, returned to the heat exchange zone for countercurrent flow against the refrigerant flowing therethrough from the condensation zone to the expansion zone, and finally returned to the compression zone. The natural gas is directed to the heat exchange zone and liquefied therein by countercurrent flow against the cold refrigerant stream flowing from the expansion zone to the compression zone. The refrigerant is made up of C.sub.1 to C.sub.5 hydrocarbons plus nitrogen as an optional constituent with the relative proportions of the constituents being controlled so that the combined cooling curve of the hot refrigerant stream and the feed gas closely matches the heating curve of the cold refrigerant stream in a sense that the curves are in close proximity at the lowest temperature levels thereof and relatively uniformly and slowly diverge as the highest temperature points on the curves are approached.

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Kansas City, MO, United States of America

Leonard K Swenson