# US 5,707,444 A · Method for controlling the temperature in a kiln

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- Number: US 5,707,444 A
- Document ID: US5707444A
- Status: Granted
- Kind: A
- Application number: 08/716,400
- Filed: 1996-09-20
- Granted: 1998-01-13
- Earliest claimed: 1994-04-21
- Assignees: F. L. Smidth & Co. A/S
- Inventors: S.o slashed.ren Hundeb.o slashed.l
- Web page: https://patentgrep.com/patent/US5707444A

## CPC

- F27B 7/42: Arrangement of controlling, monitoring, alarm or like devices
- C04B 7/361: {Condition or time responsive control in hydraulic cement manufacturing processes (controlling or regulating in general G05; F27B7/42 takes precedence)}
- Y02P 40/121: Energy efficiency measures, e.g. improving or optimising the production methods
- F27B: FURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- C04B: LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE {(roofing granules E04D7/005)}; CERAMICS (devitrified glass-ceramics C03C10/00); REFRACTORIES; TREATMENT OF NATURAL STONE
- Y02P: CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS

## Abstract

A method and apparatus for controlling the temperature in a kiln in which cement clinker is manufactured. The temperature is controlled by controlling the fuel rate to the kiln. The fuel rate is adjusted according to a calculation that is made of the sulphur evaporation in the kiln, thereby obtaining a measure of the instantaneous temperature in the burning zone. The evaporation factor is calculated on the basis of measurements of the sulphur content in the cyclone material which passes to the kiln or a measurement of the sulphur content in the exit gases out of the kiln.

## Claims

### Claim 1

A method for controlling the temperature in a kiln for manufacturing cement clinker wherein raw materials are first preheated in a preheater by exhaust gas from the kiln, and thereafter fed into the kiln, and further wherein sulfur circulates between the kiln and the preheater in the form of sulfur dioxide in the exhaust gas from the kiln to the preheater where it is absorbed or adsorbed on basic raw feed material in the preheater and returned to the kiln in a solid state with the raw material, said method further comprising measuring the temperature in the kiln by measuring relative to time (t) the amount of sulfur (S.sub.feed) in the exhaust gas from the kiln or the amount of sulfur (S.sub.cyc) in the raw material fed to the kiln so as to obtain an evaporation factor E, the evaporation factor E being the fraction of the sulfur (S.sub.cyc) that is converted in the kiln to sulfur (S.sub.feed), said evaporation factor E then being adjusted and maintained within a set range by adjusting the amount of fuel to the kiln.

### Claim 2 (depends on 1)

A method according to claim 1, further comprising measuring the sulphur content S.sub.kiln gas (t) in the exit gas of the kiln.

### Claim 3 (depends on 1)

A method according to claim 1, further comprising measuring the sulphur content S.sub.cyc (t) in the feed stream of material to the kiln.

### Claim 4 (depends on 1, 2, 3)

A method according to any one of claim 1, 2 or 3, wherein the temperature in the burning zone of the kiln is within the range 1100.degree.-1500.degree. C.

### Claim 5 (depends on 1, 2, 3)

A method according to any one of claims 1, 2 or 3, wherein the temperature in the burning zone of the kiln is within the range 1100.degree.-1350.degree. C.

### Claim 6 (depends on 1, 2, 3)

A method according to any one of claims 1, 2 or 3, wherein the temperature in the burning zone of the kiln is within the range 1275.degree.-1325.degree. C.

### Claim 7

A plant for manufacturing cement clinker comprising a preheater for preheating cement raw meal, optionally a calciner for calcining the preheated raw meal, and a kiln for burning the preheated and optionally calcined raw meal, and wherein the temperature in the kiln is adjusted by varying the fuel rate to the kiln and wherein a meter is fitted between the kiln and the preheater for measuring relative to time (t) the amount of sulfur (S.sub.feed) in the exhaust gas from the kiln or the amount of sulfur (S.sub.cyc) in the raw material fed to the kiln so as to obtain an evaporation factor E, the evaporation factor E being the fraction of the sulfur (S.sub.cyc) that is converted in the kiln to sulfur (S.sub.feed), said evaporation factor E then being adjusted and maintained within a set range by adjusting the amount of fuel to the kiln.

### Claim 8 (depends on 7)

A plant according to claim 7 wherein the meter is located in the exit gas duct of the kiln.

### Claim 9 (depends on 7)

A plant according to claim 7, wherein the meter is located in the feed stream duct to kiln.