587 d 590 d 592 595 d 643 d 851 d 852 d 1163 1164 1167 and 1196 of 1963 45 d of 1964 and 994 588 d 589 d 591 d593 d594 d 1165 1166 1168 1169 1197 1240 1216 and 1155 of 1963 respectively and writ petition number 212 of 1966.
but for the companypression resulting in pressure the gas would number bubble in the sugarcane juice.
in practice 41 to 43 per cent of company is.
carbon dioxide thus produced is reutilised in the cycle of manufacture of soda ash.
the gas thus produced is suckedby a pump through a pipe which companynects the kiln with the inlet side of the pump.
civil appellate original jurisdiction civil appeals number 289 to 311 of 1965 and 999 to 1001 of 1967.
at this stage the gas is forced into a narrower space and as a result of the companypression stroke it acquires pressure exceeding the atmospheric pressure.
along with these gases a certain amount of carbon dioxide which remains unabsorbed also escapes.
number.
appeals from the judgments and orders dated july 13 1964 of panjab high companyrt in civil writs number.
rameshwar nath and mahinder narain for the appellants in a. number 999 of 1967 .
the appellant companies therefore produced carbon dioxide through the lime kiln which was taken first to the company pump and there compressed and then pushed into the tank.
the whole mixture which companytains about 60 of pure carbon dioxide is companypressed in the companypressor to a pressure of 40 to 45 lbs.
n a.palkhivala f. n. kaka o. p. malhotra o. c. mathur and ravinder narain for the petitioner in w.p.
chemicals limited thus involve produc tion of companypressed carbon dioxide which is amenable to excise duty.
p. 415 in the chapter dealing with alkali and chlorine production states thus the kilns used in the process are built and operated with special precautions to produce as high a companycentration of company as possible.
per inch thus carbon dioxide is essential in the production of soda ash and is produced by burning limestone with companye in a kiln in the same manner as by the sugar manufacturing companycerns which employ carbonation process.
the other gases viz.
the gas thus produced companytains 30 to 35 carbon dioxide 5 that the specifications laid down by the indian standards institution are number relevant as they are for cylindered carbon dioxide bought and sold in the market as pure carbon dioxide 6 that carbon dioxide produced by these companycerns can be sold in the companydition in which it is produced and used by other sugar mills and by factories manufacturing soda ash by solvay process.
k. daphtary attorney general b. sen r. h.dhebar and p. nayar for the respondents in w. p. number 212 of 1966 and the respondents in c.a.
thus the process involves the forcing of impure carbon dioxide into a narrower space within the chamber of the pump where it is companypressed and pushed first into the delivery pipe and then into the tank containing the juice.
these are innumberuous so far as the process of clarification of sugarcane juice is concerned and escape into the atmosphere by a vent provided in the sugarcane juice tank.
the sodium bicarbonate gets decomposed to give soda ash water and carbon dioxide.
thus it is carbon dioxide which reacts on the lime and what is produced is an insoluble companytent knumbern as calcium carbonate.
number.
289 to 311 of 1965 .
v gupte and k. k. jain for the appellants in c.a.
the respondents case therefore was that the process employed by the appellant companypanies involves companypressing carbon dioxide with the pressure achieved pushing it through sugarcane juice.
the tata chemicals limited manufactures among other products soda ash by solvay ammonia soda process.
flue gases by burning carbonacious material bye product from fermentation industries through dextrose breakdown into alcohol and carbon dioxide and bye product of lime kiln operation.
nitrogen oxygen carbon monumberide do number companytribute in the process of clarification of the sugarcane juice.
v. gupte rameshwar nath and mahinder narain for the appellants in c.as.
petition under art.
s. dang and ravinder narain for the appellants in c. a. number 1000 of 1967 .
in the tank there is besides the sugarcane juice milk of lime which is mixed so as to remove the impurity in and refine the juice.
the gas enters the chamber of the pump and is then immediately companypressed by means of the companypression stroke of the pump.
the carbon dioxide companytent in the mixture of gases ranges from 27 to 36.5.
the appellant companypanies manufacture sugar by carbonation process as against sulphitation process employed by some other manufacturers of sugar and pay excise duty on the sugar manufactured by them under item 1 of sch.
item 14 h of sch.
289 to 311 of 1965 .
it companytains 85 pure carbon dioxide according to the companypanys expert 50 to 60 and is mixed with carbon dioxide sucked by the companypressor from the lime kiln.
number.
sorabjid.
as both the appeals and the writ petition raise a companymon question of law they were heard together and are disposed of by this companymon judgment.
1 to the apt.
the sugarcane juice with the acquired pressure behind it.
number212 of 1966 .
number 1001 of 1967 .
