Process and plant for the purification of raw gases by means of physical gas scrubbing

Patent metadata

Field	Value
Publication number	US-10464012-B2
Application number	US-201615546311-A
Country	US
Kind code	B2
Filing date	Jan 19, 2016
Priority date	Jan 30, 2015
Publication date	Nov 5, 2019
Grant date	Nov 5, 2019

Abstract

A process for separating undesired, in particular acidic gas constituents from a raw gas, in particular raw synthesis gas, by absorption with cold methanol as physical detergent, wherein the methanol is cooled in a compression refrigeration machine by using a multi-component coolant. The use of the coolant according to the invention provides significant advantages with regard to the compressor capacity required in the compression refrigeration machine for the provision of a defined cooling capacity.

First claim

The invention claimed is:

1. A process for the separation of undesired gas constituents, comprising carbon dioxide and hydrogen sulfide, from a raw synthesis gas, with methanol as detergent, the process comprising the following steps:
a) supplying the raw synthesis gas to the absorption apparatus;
b) cooling a methanol partial stream withdrawn from the absorption apparatus by indirect heat exchange with a coolant in a heat exchanger arranged outside the absorption apparatus thereby producing a cooled methanol partial stream and recirculating the cooled methanol partial stream into the absorption apparatus, wherein the coolant is cooled in a compression refrigeration machine which includes at least one compression stage;
c) contacting the raw synthesis gas with the cooled methanol partial stream and with at least one further methanol partial stream recirculated from downstream process stages of the absorption apparatus, wherein a process gas stream depleted of undesired gas constituents and a loaded methanol partial stream enriched in undesired gas constituents is obtained;
d) multistage regeneration of the loaded methanol partial stream by pressure decrease and/or temperature increase, between or downstream of which optionally further absorption steps can be carried out for separating further undesired gas constituents from the process gas stream, wherein at least one regenerated methanol partial stream is obtained, which is recirculated to the step c) and wherein gas streams containing carbon dioxide and hydrogen sulfide are obtained, which are removed from the process;
wherein the coolant contains 5 to 15 mol-% ethylene, 5 to 15% mol-% n-butane, 30 to 40 mol-% propane and 30 to 60 mol-% propylene.

2. The process according to claim 1 , wherein the coolant and the methanol partial stream are arranged in a counter-current flow in the heat exchanger in the step b).

3. The process according to claim 1 , wherein the compression refrigeration machine includes three compression stages in which a compression of the vaporous coolant is effected thereby producing a compressed coolant vapor.

4. The process according to claim 3 , wherein the compressed coolant vapor is condensed in a first cooling stage by indirect heat exchange to form a condensate and the condensate is subcooled in a second cooling stage by indirect heat exchange against the gas stream containing carbon dioxide obtained in the step d) thereby forming a subcooled condensate.

5. The process according to claim 4 , wherein the subcooled condensate is evaporated or partly evaporated in at least one evaporation stage to produce a coolant vapor, the coolant vapor is further cooled, and the coolant vapor thus further cooled down is used for cooling the methanol partial stream in the step b).

6. The process according to claim 1 , wherein the cooled methanol partial stream is cooled to a temperature between −35° C. to −25° C. in the step b).

7. The process according to claim 1 , wherein the raw synthesis gas is supplied to the absorption apparatus at a temperature between −5° C. and 0° C. during the step a).

Assignees

• Air Liquide

Inventors

• Chaubet Lucie
• Wagner Marc

Classifications

• C10K1/004

  Sulfur containing contaminants, e.g. hydrogen sulfide · CPC title

• F25J2205/50

  using absorption, i.e. with selective solvents or lean oil, heavier CnHm and including generally a regeneration step for the solvent or lean oil · CPC title

• F25J3/08

  Separating gaseous impurities from gases or gaseous mixtures {or from liquefied gases or liquefied gaseous mixtures}(cold traps B01D8/00) · CPC title

• C09K2205/12

  Hydrocarbons · CPC title

• B01D2257/504

  Carbon dioxide · CPC title