A method for converting a low pressure distillate hydrotreating process unit to a high pressure distillate hydrotreating process unit, which low pressure process unit comprises: i) a pump for introducing a distillate feedstream to the hydrotreating process unit; ii) a heat exchanger comprised of a first passageway contiguous to but not in fluid communication with a second passageway, wherein said first passageway is in fluid communication with said pump; iii) a furnace containing tubes having a first end and a second end and designed for pressures up to 500 psig ( 3.4 MPag) and through which distillate feedstream can flow, which tubes have an effective surface area to heat the feedstream to a predetermined reaction temperature and wherein the first end of said tubes is in fluid communication with said first passageway of said heat exchanger and the second end of said tubes is in fluid communication with the inlet of reactor of c) below; iv) a reactor designed for operating pressures not exceeding 500 psig (3,4 MPag) and which reactor has an inlet in fluid communication with the second end of said tubes of said furnace and an outlet for removing product, which outlet is in fluid with said second passageway of said heat exchanger; v) a separator vessel having an inlet in fluid communication with said second passageway of said heat exchanger, said separator having a first outlet for removing vapor phase components and a second outlet for removing a liquid phase product stream; vi) a stripper in fluid communication with said second outlet of said separator vessel; and vii) a low pressure recycle compressor having an inlet and an outlet and wherein said inlet is in fluid communication with the first outlet of said separator vessel and wherein said outlet of said compressor is in fluid communication with the first end of said furnace tubes, which compressor is capable of an outlet pressure of up to 500 psig (3.4 MPag); which method comprises: a) installing a high pressure pump between said heat exchanger and said furnace, which pump is capable of pumping a liquid feed to a pressure up to 1,500 psig (10.3 MPag); b) replacing the furnace tubes with tubes that can withstand pressures up to 1,500 psig (10.3 MPag); c) replacing said reactor with a reactor designed for pressures up to 1,500 psig (10.3 MPag); d) installing a high pressure letdown valve at the outlet of the reactor capable of reducing the pressure of a feedstream from a pressure of 1,500 psig ( 10.3 MPag) to a pressure less than 500 psig ( 3.4 MPag); and e) replacing the low pressure recycle compressor with a high pressure compressor, or in the alternative adding a high pressure compressor in series with the recycle compressor, which high pressure compressor is capable of compressing a vapor stream to a pressure up to 1,500 psig ( 10.3 MPag). i) a pump for introducing a distillate feedstream to the hydrotreating process unit; ii) a heat exchanger comprised of a first passageway contiguous to but not in fluid communication with a second passageway, wherein said first passageway is in fluid communication with said pump; iii) a furnace containing tubes having a first end and a second end and designed for pressures up to 500 psig ( 3.4 MPag) and through which distillate feedstream can flow, which tubes have an effective surface area to heat the feedstream to a predetermined reaction temperature and wherein the first end of said tubes is in fluid communication with said first passageway of said heat exchanger and the second end of said tubes is in fluid communication with the inlet of reactor of c) below; iv) a reactor designed for operating pressures not exceeding 500 psig (3,4 MPag) and which reactor has an inlet in fluid communication with the second end of said tubes of said furnace and an outlet for removing product, which outlet is in fluid with said second passageway of said heat exchanger; v) a separator vessel having an inlet in fluid communication with said second passageway of said heat exchanger, said separator having a first outlet for removing vapor phase components and a second outlet for removing a liquid phase product stream; vi) a stripper in fluid communication with said second outlet of said separator vessel; and vii) a low pressure recycle compressor having an inlet and an outlet and wherein said inlet is in fluid communication with the first outlet of said separator vessel and wherein said outlet of said compressor is in fluid communication with the first end of said furnace tubes, which compressor is capable of an outlet pressure of up to 500 psig (3.4 MPag); a) installing a high pressure pump between said heat exchanger and said furnace, which pump is capable of pumping a liquid feed to a pressure up to 1,500 psig (10.3 MPag); b) replacing the furnace tubes with tubes that can withstand pressures up to 1,500 psig (10.3 MPag); c) replacing said reactor with a reactor designed for pressures up to 1,500 psig (10.3 MPag); d) installing a high pressure letdown valve at the outlet of the reactor capable of reducing the pressure of a feedstream from a pressure of 1,500 psig ( 10.3 MPag) to a pressure less than 500 psig ( 3.4 MPag); and e) replacing the low pressure recycle compressor with a high pressure compressor, or in the alternative adding a high pressure compressor in series with the recycle compressor, which high pressure compressor is capable of compressing a vapor stream to a pressure up to 1,500 psig ( 10.3 MPag).