SU1317173A1 - Liquid neutralizer - Google Patents

Abstract

The invention relates to engine construction and allows for increased efficiency. The body 1 of the neutralizer is divided into two sections communicating with each other through the liquid through the filter element 7 and the volume of the pallet 9. The output and inlet pipes 10 and 11 are led to section A. . In the upper part of section A, a droplet separator 15 is installed with a pallet 16 connected by a channel 17 with the lower part of a pallet 9. Pipeline 11 is connected by pipeline 23 to section B. Pipeline 23 is equipped with a mechanism for controlling its penetration into the liquid. Last, hit the neck of the Venturi tube, crushed. There is an intensive mass and heat exchange of liquid and gases. The latter are cooled and cleaned from toxic substances (soot). In the droplet separator 15, the contaminated droplets are collected in the pan 16 and directed through the channel 17 to the pan 9. The cleaned gases pass through the heat exchanger 18, where they are heated from the flow of newly introduced exhaust gases, cooling them. 5 hp f-ly, 1 ill. ate with with with fO W //

Description

FIELD OF THE INVENTION The invention relates to mechanical engineering, namely, devices for neutralizing the exhaust gases of an internal combustion engine.

The aim of the invention is to increase the efficiency of neutralization.

The drawing shows the schema of the proposed liquid catalyst.

The device contains Cornus I, filled with a neutralizing liquid and divided. When the engine is started, the pressure of the processed gases overcomes the hydrostatic pressure of the liquid column 5, increases the pressure in the gas cavity 6 to

Pr2 EGR - H, .2-p-g. (2)

where H is the fluid level in the second section. At the same time, some of the liquid from the second section is displaced to the first, where the level rises to

I., (Por -.- PB) / {pg), M (3)

partition 2 into two sections: the first AO When the engine runs at a constant liquid 3 and gaseous 4 phases in a different mode (and, consequently, when nocfo the second section B with liquid 5 and gaseous horn), the liquid level in the 6-phase 6 phases, communicating between co-A remains constant and is determined

liquid fights through filtering by ele-equality (3), and the level of Ho2 decreases,

Ment 7 and volume 8 of the pallet 9. The output, as part of the liquid supplied to the tube

thirty

pipeline O and inlet 11 are brought to section A.

The inlet piping of section A is made in the form of a Venturi tube with a diffuser part 12, directed vertically, and a throat 13 with at least one hole, which is connected to the section B liquid by a LI channel, and a droplet separator 15 is installed in the upper part of section A and connected with a pallet 16 channel 17 with the bottom of the pallet 9.

A heat exchanger 18 is installed outside the neutralizer case between the inlet 11 and outlet 10 pipelines. The neutralizer housing is equipped with valves 19-22 for draining, filling, draining and flushing the neutralizer. The inlet pipe 11 (after the heat exchanger 18 or before it) is connected by a relatively thin additional pipe 23 to the second section B, and which it is inserted from top to bottom so that its open cut 24 is at the level of the inlet channel 14. The additional pipe 23 is equipped with a mechanism 25, It is appropriate to change the level of penetration into the fluid of its slice.

Liquid neutralizer works as follows.

With the D1) open, the drain valve 21 of the casing-40 of the neutralizer 1 is filled through the ventilator. til 20 (valve 19, in the case of liquid purified from mechanical impurities) neutralizing liquid to the level

H3 APor / (, g) - (P r r - p6) / (p.g), m (D) where Dfrg, N / m, (determined by the mode of operation of the engine); RP. .-- gas pressure at the location of the additional pipeline 23 to the pipeline P,

Р gas pressure in the volume of 4 sections A, N / m;

Р - working fluid density, kg / m;

Pb - barometric pressure, N / m. 55 The water level is calculated from the slice 24 tr. bg 1 conduit 23. Before starting digigatol ng (. the valves are closed, in gas ps. uetn (section B is barometric pressure

Venturi is carried with gases into the atmosphere. At the same time, the pressure Рг2 increases according to (2) due to the bubbling of a small part of the gases through the liquid layer On and on (the gas cavity 6 has them), and the pressure in the liquid at the level of the throat of the Venturi nozzle does not change and is equal to or Horn, if section 24 is at the throat level, or greater than the EGR, if the slice is above the throat or less, if slice 24 is below the throat level. Thus, at a constant EGR, the pressure at which fluid is supplied to the throat of the Wemturi tube through the supply channel 14 does not depend on the amount of water with the exhaust gases into the atmosphere (or similarly from the water level in section B), therefore, the flow rate of the fluid supplied to the venturi throat remains unchanged as long as the water level in the second section drops to either cut off 24 or venturi pipe necks.

- the need to increase the flow rate of the fluid supplied to the Venturi, the tube 23 should be raised by means of the mechanism 25, and otherwise lowered. The liquid, G1ol; and Aem in the throat of the Venturi tube, is crushed into small ki & pli with a large total surface, on which n) there is also a fuel: i) the mass-heat exchange of the liquid phase and gases, as a result of which the gases are cooled and very - from toxic substances, soot. In the dropping element 15, the contaminated droplets are collected in the sump 16 and directed through channel 17 to the sump 9. After the droplet separator 5, the cleaned relatively cold gases flow through the heat exchanger 18, where they are heated by the flow of the re-flowing gases, cooling them . Cooling of the exhaust gases interacting with the neutralizing liquid leads to a decrease in its entrainment in the vapor phase to the atmosphere, and the heating of the gases released into the atmosphere from the heat exchanger 18, yMeHbHjaeT, their relative humidity. In case of possible water leaks, for example, during the engine stop, the filter element 7 preventively popalaiin; soot accumulated in section L and pallet

45

50

Lenna. When the engine is started, the pressure of the processed gases overcomes the hydrostatic pressure of the liquid column 5, increases the pressure in the gas cavity 6 to

Pr2 EGR - H, .2-p-g. (2)

where H is the fluid level in the second section. At the same time, some of the liquid from the second section is displaced to the first, where the level rises to

I., (Por -.- PB) / {pg), M (3)

During engine operation at all times as part of the fluid supplied to the tube

0

0

five

Venturi is carried with gases into the atmosphere. In this case, the pressure Pr2 increases according to (2) due to the bubbling of an insignificant part of the gases through the fluid layer On and On (the gas cavity 6 of the gas cavity 6, and the pressure in the fluid at the throat level of the Venturi nozzle does not change and is equal to or Horn, if the cut is 24 is at the throat level, or greater than the EGR, if the slice is above the throat or less, if slice 24 is below the throat level. Thus, at a constant EGR, the pressure at which fluid is supplied to the throat of the Wemturi tube through the supply channel 14 does not depend on the amount of water with exhaust gases into the atmosphere (or similarly from the water level in section B), therefore, the flow rate of the fluid supplied to the venturi throat remains unchanged as long as the water level in the second section drops to either cut 24 or venturi pipe necks.

- the need to increase the flow rate of the fluid supplied to the Venturi, the tube 23 should be raised by means of the mechanism 25, and otherwise lowered. The liquid, G1ol; and Aem in the throat of the Venturi tube, is crushed into small ki & pli with a large total surface, on which n) there is also a fuel: i) the mass-heat exchange of the liquid phase and gases, as a result of which the gases are cooled and very - from toxic substances, soot. In the dropping element 15, the contaminated droplets are collected in the sump 16 and directed through channel 17 to the sump 9. After the droplet separator 5, the cleaned relatively cold gases flow through the heat exchanger 18, where they are heated by the flow of the re-flowing gases, cooling them . Cooling of the exhaust gases interacting with the neutralizing liquid leads to a decrease in its entrainment in the vapor phase to the atmosphere, and the heating of the gases released into the atmosphere from the heat exchanger 18, yMeHbHjaeT, their relative humidity. In case of possible water leaks, for example, during the engine stop, the filter element 7 preventively popalaiin; soot accumulated in section L and pallet

five

0

bottom, in section B, from where water is supplied for gas irrigation. As soot accumulates in the pallet 9, it can be mechanically cleaned when removed or by a jet of water supplied through the valve 22 and exiting through the valve 20.

Claims (6)

Invention Formula . Exhaust gas neutralizer of an internal combustion engine, comprising a housing equipped with inlet and outlet pipes, partially filled with a neutralizing liquid and separated by a partition recessed into the last, first and second sections, and a cage separator, the inlet pipeline being made in the form of a Venturi pipe and connected by means of a supply channel with one of the sections below the liquid level, characterized in that, in order to increase efficiency, it additionally contains a filter pan conductive element mounted in the lower housing part, an inlet conduit connected at - the help of the inlet channel with the second section and in the latter is placed an additional pipeline, on one side buried in the liquid to the level of the inlet channel, and on the other side connected to the inlet pipe above the inlet channel along the exhaust gases. 2. A neutralizer according to claim J, characterized in that the diffuser portion of the venturi tube 0 is located vertically, and its cut is placed above the level of the neutralizing liquid of the first section. 3. The neutralizer according to Claim 1, characterized in that a portion of the output pipeline is once in the inlet pipeline. 4. The neutralizer PP. 1-3, characterized in that the second section is sealed. 5. Neutralizer on PP. 1-4, characterized in that the additional pipeline of the second section is provided with a mechanism for controlling its penetration into the liquid. 6. The neutralizer PP. I-5, characterized in that the additional pipeline is connected to an external source of adjustable pressure.