Device for converting alcohols to ethers

Claim 1

A compression ignition engine capable of running on a fuel of methanol and dimethyl ether, said engine comprising a compression ignition engine having at least one cylinder, a heat exchanger mounted by mounting means on the compression ignition engine, said heat exchanger being adapted to heat methanol passing therethrough to a temperature in the range of 80° to 400° C., a conversion chamber containing a catalyst for converting methanol to dimethyl ether at a temperature in the range of 80° to 400° C., also mounted by mounting means on the compression ignition engine, a supply tank for methanol, a first pipeline to lead a stream of methanol from the supply tank to the cylinder, a second pipeline to lead a stream of the methanol from the supply tank to the heat exchanger, a pipe for the methanol vapour leading from the heat exchanger to the conversion chamber, and a pipe for the dimethyl ether leading from the conversion chamber to the cylinder.

Claim 3

A method of running a compression ignition engine on methanol and dimethyl ether, which comprises supplying a first part of methanol fuel from a supply tank containing the methanol fuel through a first pipe to a cylinder of the engine, and supplying a second part of the methanol from the supply tank through a second pipe to a heat exchanger where it is heated to a temperature in the range of 80° to 400° C., supplying this second part of the methanol at a temperature in this range from the heat exchanger to a catalytic conversion chamber containing a catalyst capable of converting the methanol to dimethyl ether at a temperature in the range of 80° to 400° C. and leading the dimethyl ether formed directly to the cylinder.

Claim 4

A method of running a compression ignition engine on methanol and dimethyl ether, which comprises supplying a first part of methanol fuel from a supply tank containing the methanol fuel through a first pipe to a cylinder of the engine, and supplying a second part of the methanol from the supply tank through a second pipe to a heat exchanger where it is heated to a temperature in the range of 80° to 400° C., supplying this second part of the methanol at a temperature in this range from the heat exchanger to a catalytic conversion chamber containing a catalyst capable of converting the methanol to dimethyl ether at a temperature in the range of 80° to 400° C. and leading the dimethyl ether formed directly to the cylinder.