System and method for operating a liquid gas evaporator

Patent metadata

Field	Value
Publication number	US-10174935-B2
Application number	US-201514738050-A
Country	US
Kind code	B2
Filing date	Jun 12, 2015
Priority date	Jul 8, 2014
Publication date	Jan 8, 2019
Grant date	Jan 8, 2019

Abstract

A system (1) and method for operating a liquid gas evaporator (3), comprising an evaporator (3), a trough (5) carrying the evaporator (3), a housing (7) which surrounds the evaporator (3) on three sides, at least one detector (9) for sensing liquid gas arranged in the trough (5), a line (11) for the distribution of vapor D on the fourth, non-housed side of the evaporator (3) arranged at the margin of the trough (5) which is not closed off by the housing (7), a feed (13), connected to the line (11), and a regulating valve (15) provided on the feed (13) and connected to the detector (9) and at least one shut-off valve (17).

First claim

The invention claimed is:

1. A liquid gas evaporator system comprising:
a liquid gas evaporator for evaporating a liquid gas into its gaseous aggregation state,
a trough carrying the liquid gas evaporator,
a housing disposed on the trough that has an open top side, three side walls that surround the liquid gas evaporator, and an open side disposed between the side walls, the open top side and the trough, wherein the open side of the housing forms a non-housed side of the liquid gas evaporator,
at least one detector, arranged in the trough, for detection of the liquid gas and its gaseous aggregation state,
a line for distribution of vapor D, which is provided on the non-housed side of the liquid gas evaporator, wherein the line has orifices for spraying the vapor D outside the line, configured such that upon exiting the line, the vapor D travels vertically upward relative to the line,
a feed, connected to the line, for running the vapor D into the line,
a regulating valve provided on the feed, wherein the regulating valve is connected to the at least one detector, and
at least one shut-off valve that prevents a further feed of the liquid gas to the evaporator in the event of a leakage.

2. The system of claim 1 , wherein the line extends over an entire width of the non-housed side of the liquid gas evaporator.

3. The system of claim 1 , wherein the line has orifices at intervals that are oriented essentially vertically upward.

4. The system of claim 1 , wherein the non-housed side of the liquid gas evaporator is oriented to face away from a plant for processing of the liquid gas or of its gaseous aggregation state.

5. The system of claim 1 , wherein the system is arranged to be elevated in relation to a plant for processing of the liquid gas or of its gaseous aggregation state.

6. A method for operating the system of claim 1 , the method comprising:
a) evaporating a liquid gas into its gaseous aggregation state in the evaporator,
b) detecting a concentration of the liquid gas or of its gaseous aggregation state in the trough carrying the evaporator,
c) upon the detection of a predetermined critical concentration value of the liquid gas or of its gaseous aggregation state in the trough, actuating the regulating valve on the feed and consequently introducing vapor D into the line and closing the liquid gas feed to the evaporator by the at least one shut-off valve,
d) spraying the vapor D out of orifices in the line, and
e) forming a vapor curtain above the line on the non-housed side of the evaporator.

7. The method of claim 6 , wherein the vapor curtain is formed at least over an entire width of the non-housed side of the evaporator.

8. The method of claim 6 , wherein a liquid material forms during evaporation, a heavy gas that collects in the trough.

9. The method of claim 6 , wherein the vapor D is fed with a pressure of at least 4 bar into the line.

10. The method of claim 6 , wherein the vapor D is fed with a pressure of from 10 bar to 35 bar into the line.

11. The method of claim 6 , wherein by the spraying of the vapor D in d), air is sucked in from outside the system and the liquid gas or its gaseous aggregation state is entrained out of the trough, thereby diluting the concentration of the liquid gas or the concentration of its gaseous aggregation state to a noncritical value.

Assignees

• Basf Se

Inventors

• Hammon Ulrich
• Walter Thomas

Classifications

• F17C2225/035

  High pressure, i.e. between 10 and 80 bars · CPC title

• F17C2227/0393

  using a vaporiser · CPC title

• F17C2225/036

  Very high pressure, i.e. above 80 bars · CPC title

• F22B1/021 Primary

  with heating tubes in which flows a non-specified heating fluid (for nuclear reactors F22B1/023) · CPC title

• B01D1/0082 Primary

  Regulation; Control · CPC title