EP0471060A1

EP0471060A1 - Method and system for crushing and drying a solid fuel.

Info

Publication number: EP0471060A1
Application number: EP91905840A
Authority: EP
Inventors: Daniel Fontanille
Original assignee: Stein Industrie SA
Current assignee: Stein Industrie SA
Priority date: 1990-03-06
Filing date: 1991-03-06
Publication date: 1992-02-19
Anticipated expiration: 2011-03-06
Also published as: ES2041558T3; JP3003872B2; DE69100107T2; EP0471060B1; ATE90440T1; DK0471060T3; US5191724A; DE69100107D1; JPH04505652A; WO1991014133A1

Abstract

PCT No. PCT/FR91/00180 Sec. 371 Date Oct. 29, 1991 Sec. 102(e) Date Oct. 29, 1991 PCT Filed Mar. 6, 1991 PCT Pub. No. WO91/14133 PCT Pub. Date Sep. 19, 1991.An adjustable temperature gas feed is available that feeds firstly the grinder and secondly pre-drying means. At the outlet from the grinder, the gas that has passed through the grinder is combined with the gas that has passed through the pre-drying means to convey the ground material. The total gas flow rate QA at the oulet lies between a minimum flow rate and a maximum flow rate, and the flow rate Q1 of the gas passing through the grinder (1) is proportional to the quantity Qc of material placed in the grinder. According to the invention, a temperature T to be reached by the gas outlet temperature is set (optionally as a function of the moisture content of the material), and the gas feed is adjusted in such a manner that the feed gas is as hot as possible with the quantity of gas passing through the pre-drying means being limited to as little as possible. The method adapts to the material having different moisture contents and improves efficiency while leading to combustion with low NOx.

Description

Grinding and drying method and system for solid fuel

The present invention relates to a _ζ adjustment process operation of a crushing apparatus of a solid combustible material of variable moisture content and drying said material, said apparatus being fed with material via pre-drying means, in which there is a gas supply whose temperature can be adjusted over a range, the gas

10 supply being separated into two fractions, a fraction of the gas passing through the grinding apparatus and the other fraction of the gas being sent to the pre-drying means, adjusting the flow rate Q of the fraction of gas passing through l device proportional to the flow rate Q of the material to be ground, the fraction of gas passing through the

15 the pre-drying means being combined with the fraction of gas leaving the apparatus with the ground material and all of the gas with the ground material being sent into the transport pipes, the temperature T of the gas and the ground material is measured in said transport pipes, the temperature of the gas is adjusted

20 supply as a function of the difference between a fixed temperature T- and the temperature T measured so that the measured temperature T approaches T, the flow rate of the gas fraction Q _? supplying the pre-drying means being adjusted so that the total gas flow rate Q. in the transport pipes is between a minimum flow rate ς Q. and a maximum flow rate Q. „.

^ΔD Am AM

Such a process is described in the article by VERGNIOL "A single shredder by direct heating boiler" published in the French review "Revue Alsthom" n ° l, 1985 pages 31 to 40.

In the known method, the adjustment is provided for a combustible material having the highest degree of humidity which can normally be used in the boiler considered.

The flow in the outlet pipes must be at least equal to a minimum flow because below the crushed material is no longer transported correctly. On the other hand, this flow cannot exceed a

35 maximum flow rate because above the pipes are damaged by erosion.

It follows that for a whole range of combustible material with a humidity lower than the material for which the boiler is regulated, one will be led to obtain the desired outlet temperature to add c too much gas in the pre-drying means and to lower the supply gas temperature which leads to poor efficiency.

On the other hand, the inventor has found that it is advantageous, when the quantity of ground material is increased to the maximum possible of 10, to regulate the flow rate of the fraction of pre-drying gas Q as low as possible. that the total gas flow Q. within

Ά transport piping is equal to or very little higher than minimum flow rate Q. as long as possible and then deviates from it if necessary by the smallest possible quantity. • J5 The yield obtained is also increased and moreover combustion takes place with a reduced formation of nitrogen oxides.

The method according to the invention is characterized in that a temperature of the mixture of gas and ground material T is set below T. and which can depend on the moisture content of the material and in that

20 that when the minimum gas flow rate is not sufficient to reach the fixed temperature T _p , with the temperature of the supply gas brought to the maximum of the range, the flow rate of the gas fraction Q- is increased

2 sent to the means for pre-drying the quantity necessary to reach the temperature T _? . The invention also relates to a system for grinding a solid combustible material of variable moisture content and for drying this material, comprising a grinding and drying apparatus, means for feeding material, pre-drying means arranged at following supply and supply means

The apparatus of material of the first gas injection means in the apparatus of the second gas injection means in the pre-drying means, gas supply means, said gas being separated into a first fraction feeding the first injection means and a second fraction supplying the second injection means,

35 means for adjusting the gas temperature of the supply means in a given range, transport pipes supplied with the mixture of gas from the pre-drying means and gas with the ground material from the device, means for adjusting the first injection means for adjusting the flow rate Q- of the fraction of gas passing through the apparatus in proportion to the quantity of material to be ground, means for measuring the temperature T of the gas mixture of ground material in the transport pipes, means for adjusting the temperature of the gas of the means d supply as a function of the difference between a fixed temperature T- and the temperature T measured so that T approaches T, means for adjusting the second injection means so that the total gas flow Q. in the transport piping is between a minimum flow rate Q. and a

Am maximum flow rate Q. „characterized in that the means for adjusting the second injection means are controlled on the one hand by a signal dependent on Q. so that the total gas flow rate Q. is equal to Q. when the gas outlet temperature T is greater than the temperature T „less than T., T„ being able to be chosen as a function of the humidity of the material and on the other hand, by a signal depending on the difference between the temperature T measured and the temperature T „, when T is less than T., so as to increase the flow rate of the gas fraction Q _? sent to the means for pre-drying the quantity necessary for the outlet temperature to reach T _? without, however, the total flow Q. exceeding the maximum flow Q _AM "

There is described below, by way of example and with reference to the figures of the appended drawing, a method of adjusting the operation of a coal mill with variable humidity content, of horizontal axis as well as a system for the implementation of the process.

Figure 1 shows schematically the whole system. FIG. 2 represents the regulation of the air flow as a function of the coal flow according to the known method and devices.

FIG. 3 represents the regulation of the air flow as a function of the coal flow according to the method of the invention.

In FIG. 1, the rotary ball mill 1, with a horizontal axis, rotates in pins 1A, 1B, at the same time ensuring the supply of coal and drying air. Total air flow supply is measured by the flow meter 2. The temperature T of the air charged with powdered carbon is measured at the outlet of the mill in the transport pipes 10 and 11 by the sensor 3. The air flow Q- introduced in the mill by its pins through the conduits 38A, 38B is regulated by valves 4A-4B with regulators 37 'with proportional-integral control.

These regulators 37 ′ are controlled by the member 37 for displaying the load request of the boiler supplied with ground coal. On the other hand, a microprocessor 35, controlled by the indications of the sensor 3 through the minimum temperature 32 (proportional-integral control) and maximum 33 and minimum 34 air flow setpoints, regulated by the valves 30 and 31 arranged on conduits 39, 40 the flow rate of the air fraction (bypass air) Q_ sent directly to the separators 8,9 through the mixing boxes 16-17. The flow air fraction Q _p ensures in these boxes 16, 17 preheating and pre-drying of the material.

The supply air used for drying and transport is discharged by the fan 20. A portion is heated in a heat exchanger 21 which at the same time ensures the heating of a fraction of secondary air discharged by the fan 20A and sent directly to the burners of the boiler hearth. Another part is not heated and bypasses this exchanger by the conduit 23. The respective flow rates of hot air and cold air are regulated by the valves 24 and 25, controlled by the microprocessor 36 with proportional-integral control with reference 36A temperature, controlled by the sensor 3 of the temperature of the air charged with powdered coal at the outlet of the mill. The cold air and hot air flows are mixed in the pipe 26 provided with a closing valve 27. The pipe 26 is separated into two pipes 28, 29, the pipe 28 separating into two pipes 38A and 39 and the conduit 29 separating into two conduits 38B and 40.

The coal to be ground, poured into the hoppers 12 and 13, is sent by the feeders 14 and 15 into the mixing boxes 16 and 17, where it is added with the fraction of air not introduced into the grinder arriving via the conduits 28 , 29. It flows towards the crusher through the pipes 18 and 19, then enters them through the pins 1A and 1B coaxially with the fraction of air introduced into it by the valves 4A, 4B controlled by regulators 37 'with proportional-integral action receiving an order from the display organ 37

-. of the boiler load request, as indicated above.

The fraction of air charged with pulverized coal is evacuated from the crusher through the pins 1A and 1B, then after addition of the fraction of bypass air from the mixing boxes 16 and 17, - by the conduits 6 and 7 to the separators 8 and 9. The 0 particles of coal are divided there into coarse particles, which are recycled towards the conduits 18, 19 supplying the mill, and into fine particles, which go to the burners of the boiler hearth. The temperature of this outlet air, as indicated above, is measured by the sensor 3 and transmitted to the microprocessor 36 for fixing the temperature setpoint and controlling the respective flow rates of the hot air and cold air fractions. by valves 24 and 25.

This temperature is also transmitted to the computer 32 to develop a control signal which is a function of the difference between the _Q measured temperature and the setpoint displayed at 32A.

FIG. 2 represents the regulation of the air flow rate Q., in the transport pipes 10.11 depending on the flow rate of coal Q. vs

The air flow Q- (line segment 0E, E being the abscissa point 100) passing through the mill is proportional to the coal flow. The flow Q. must be equal to or greater than a minimum flow Q. and not exceed a maximum flow Q.. Total flow Q. Am Am A

(equal to - + Q „) as a function of Q is a horizontal segment BC of ordinate Q. then an inclined segment CD, with point D of ordinate

Q .-- and abscissa 100 (corresponding to the maximum coal flow rate

AM 0 ground).

For a flow rate Q of ground coal represented by ON on the axis 0Q, there will therefore be an air flow rate passing through the mill Q_. equal to PN (P being the point of the straight line 0E with ordinate ON) and an air flow rate Q _p passing through the pre-drying means 16 and 17 (or air of

35 bypass) equal to PR (R being the point of the ordinate CD segment WE) .

The air flow Q (PN) passing through the mill is determined by the chain 37, 37 ′ as a function of Q.

In the known system, the chain 32, 33, 34 does not exist. The _ς calculator 35 controls the valves 31, 30 so that the bypass quantity of air Q_ is equal to PR so that it always follows the broken line BCD.

This line was chosen so that the temperature of the outlet air is equal to T- for the wettest coal which it is conceivable to grind for the associated boiler, by sending the warmest supply air possible, that is to say with the valve 25 closed.

If a coal is less humid, the outlet temperature T will increase the computer 36 on which the temperature T will be displayed at 36A. It will deliver a signal to open the cold air valve 24 and close the hot air valve 25 in order to '' lower the temperature of the supply air so that the outlet air has a measured temperature which is equal to T ..

FIG. 3 represents the method according to the invention. In the _Q diagram Q, Q. there is shown the broken line BCD which corresponds to the coal of maximum treatable humidity for the boiler considered.

If the coal has a lower humidity, we decide to follow the broken line BCD '. The BC segment is longer than BC and the segment

CD 'has a slightly steeper slope than the segment BC, but for the quantity Q corresponding to the maximum of treatable carbon, a point D' is located below D and above E.

The air flow through the mill as a function of Q is always represented by the line segment OE. Thus for an ON quantity of coal the air flow Q- passing through the mill is PN 0 but only a quantity of pre-drying air Q_ equal to PR 'which is less than PR must be added to it. When you are on the OE segment (greater than Q.) the quantity Q_ is zero.

To arrive at following the line BCD ', a temperature T_ is lower than T- which is applied to the input 32A of the computer 32, the latter lets the minimum signal pass. So if T is less than 1 it is the signal corresponding to T which will pass, the instructions 33 and 34 ensure that the command sent to the computer 35 would not result in a flow Q lower than the minimum flow Q or greater than the maximum flow. _M »Flow rate Q. will increase until temperature T is reached _? which corresponds to the B'C branch.

Since the computer 36 is greater than T, the valve 24 will open the hot air valve as much as possible and the cold air valve 25 will close. Supply air having the highest temperature in the setting range is thus obtained and thanks to the computer 35 a minimum quantity Q (PR ') of this hot air is sent through the preheating means.

Thanks to the method according to the invention, the CD segment is replaced by a broken line CCD '.

It is thus possible to use the warmest supply air possible to obtain an outlet air temperature T and limit the bypass air as much as possible. In the known method instead of limiting the flow of bypass air Q _? when the coal is less humid we send the same amount of bypass air by lowering the temperature, which on the one hand is bad for the yield and on the other hand increases the total air flow Q. thus causing combustion with production of nitrogen oxides.

The drier the carbon, the longer the BC stage and the lower the point D ', keeping the same set temperature T „.

The invention relates firstly to the adjustment of the operation of a grinding apparatus for fossil fuels, such as coal, but it also applies to the grinding of non-combustible materials, such as minerals.

Claims

1) Method for adjusting the operation of an apparatus (1) for grinding a solid combustible material of variable moisture content and for drying this material, said apparatus (1) being supplied with material _c by means pre-drying (16, 17), in which there is a gas supply (20, 24, 25) whose temperature can be adjusted over a range, the gas being separated into two fractions, a fraction of the gas passing through the grinding apparatus (1) and the other fraction of the gas being sent to the pre-drying means (16,

10 17), the flow rate of the fraction of gas Q- passing through the apparatus (1) is adjusted in proportion to the quantity of material to be ground Q, the fraction of gas Q_ passing through the pre-drying means (16, 17) being combined with the fraction of gas Q- leaving the apparatus (1) with the ground material and all of the gas with the ground material being

15 sent into transport pipes (10,11), the temperature T of the gas and of the ground material in said transport pipes (10, 11) is measured, the temperature of the feed gas is adjusted as a function of the difference between a fixed temperature T. and the temperature T measured so that the measured temperature T approaches T., the

20 flow rate of the fraction of gas supplying the pre-drying means (16,

17) being adjusted so that the total gas flow rate Q. in the transport lines (10,11) is between a minimum flow rate

Q. and a maximum flow rate Q. „characterized in that an Am AM temperature of the mixture of gas and ground material T_ is set less than 25 T., T_ being able to depend on the moisture content of the material, and in that that when the minimum gas flow rate Q. is not sufficient to reach the fixed temperature T ^, with the temperature of the supply gas brought to the maximum of the range, the flow rate of the gas fraction Q „sent to the means of increase is increased pre-drying (16, 17) of the quantity necessary to reach the temperature T „.

2) System for grinding a solid combustible material of variable moisture content and for drying this material comprising an apparatus (1) for grinding and drying the material supply means (12, 13), pre-drying means (16, 17) arranged after the

35 supply means (12, 13) and supplying the device (1) with material, first means of injection. (38A, 38B) of gas in the apparatus (1), second means for injecting (39, 40) of gas into the pre-drying means (16, 17), means for supplying gas (20, 24 , 25, 26), said gas being separated into a first fraction

- supplying the first injection means (38A, 38B) and a second fraction supplying the second injection means (39, 40), means for adjusting (36) the temperature of the supply gas (20, 24, 25, 26) in a given range, transport pipes (10,11) supplied by the mixture of gas from the pre-drying means _Q (16, 17) and gas with the ground material from the device (1) , adjustment means (4A, 4B) of the first injection means (38A, 38B) for adjusting the flow rate of the fraction of gas Q- passing through the device (1) in proportion to the quantity of material to be ground Q_ , means for measuring (3) the temperature T of the gas mixture of ground material in the transport pipes (10, 11), means for adjusting (24, 25, 36) the temperature of the gas of the supply means ( 20,21) as a function of the difference between a fixed temperature T and the temperature T measured so that T approaches T-, means for adjusting ge (30, 31, 35) of the second injection means (39, _Q 40) so that the total gas flow Q in the transport pipes (10, 11) is between a minimum flow 0. and a flow

Am maximum Q _AJ - characterized in that the adjustment means (30, 31, 35) of the second injection means (39, 40) are controlled on the one hand by a signal dependent on Q so that the total flow of gas Q. 5 is equal to Q. when the gas outlet temperature T is greater than a temperature T „less than T-, T_ being able to be chosen as a function of the humidity of the material and on the other hand by a dependent signal the difference between the measured temperature T and the temperature T _p , when T is less than T _? , so as to increase 0 the flow rate of the fraction of gas G_ sent to the pre-drying means

(16, 17) of the quantity necessary for the outlet temperature to reach T_ without, however, the total flow Q exceeding the maximum flow QA.M „.

5