THE FIXED NITROGEN INDUSTRY IN CZECHOSLOVAKIA

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CIA-RDP79-01093A000400180001-5
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March 1, 1954
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r pgrove pr a ease 1999/09/0~2:CIA=RDP79-01093A000400180001-5 US 4~F-~'IALS 41~ILY 'ROVISIONAL INTELLIGENCE REPORT r~ ~`~~ ~"IX~D NITROGEN INI7US'~RY ~N C~~G~IC)S~OVAKIA ;,`CIA/RR PR-49 1 _March 1954 CENTRAL. INTE_LLIGEI~C~ AGENCY OFFICE bF RESEARCH AND CtEPORTS p~}t"UM~NO. ~--- l~C7 CHANt~E IN CLRSS. ^ ^ YSECLA551F4ED c . CLAB$? GFtdNQEb Ta: NESCT~t~VtEW~D~A`FE: F~EViEWER: 006._..-- 51-- 4 Approved For Release 1999/09/02 :CIA=RDPT9-01093A00040018000?-5 NT IAL Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 This material contains information affecting the National Defense oi' the United States within the mee,ning; of the espionage laws, Tftle 18, USC, liecs. 793 and 794, the trans- mission or revelation. of which in any rnanner to an unauthorised person is prohibited by law. Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/ ~~701093A000400180001-5 ~? 5-E- =T PROVISIONAL INTELLIGENCE REPQRT TFiE FIXED NITROGEN INDUSTRY IN CZECHOSLOVAKIA C IA ~RR PR -~+9 (ORR Project 22.1.x+) NOT ICE The data and conclusions contained in this report do not necessarily represent the final position of ORR and should be regarded as provisional only and subject to revision. Comments and data which may be available to the- user are solicited. Office of Research and Reports Approved For Release 1 3A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 CaN FI D ENTI~L coNZ~NTs summary : 1 I. History and Organization of the Industry 3 II . Supplies ~+ A. Production ~+ 1. Synthetic Ammonia : ~+ 2. Nitric Acid 6 3. Nitrogen Fertilizers 8 ~+. All Forms of Fixed Nitrogen 12 B. Stockpiling 12 C . Trade 13 D. Availability 15 III. Consumption 18 A. Synthetic Ammonia 18 B. Nitric Acid ? ? 19 C. Nitrogen Fertilizers 20 D. All Forms of Fixed Nitrogen 21 IV . Input Requirements 21 A. Synthetic Ammonia 21 B . Nitric Acid 22 C. Nitrogen Fertilizers ~. 23 1. Ammonium Nitrate 2.3 2. Ammonium Sulfate 2~+ 3. Calcium Cyanamide 26 V. Capabilities, Vulnerabilities, and Intentions 26 A. Capabilities 26 B. Vulnerabilities . ~ 28 C. Intentions 28 CONFI~F~,~ Approved For Release 1999/09/02`:-E 1093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 CONFIDENTIA Appendixes Appendix A. Fixed Nitrogen Plants in Czechoslovakia . Appendix B. Brief History and Technology of the Fixed Nitrogen Industry Appendix C . Methodology Appendix D. Gaps in Intelligence Appendix E. Sources and Evaluation of Sources . Tables 1. Administrative Organization of Synthetic Ammonia Plants in Czechoslovakia, 1952 . 2. Estimated Production of Synthetic Ammonia in Czecho- slovakia, Selected Years, 1930-5~+ . 3. Estimated Production of Synthetic Ammonia Plants in Czechoslovakia, 1953 and 1954 . 4. Page . 31 . 41 . 47 . 51 ? 53 ~+ ? 5 6 Estimated Production of Nitric Acid .in Czechoslovakia, Selected Years, 1930-5~+ 7 Estimated Production of Nitric Acid Plants in Czecho- slovakia, 1953 and 1954 8 6. Nitrogen Content of the Mayor Nitrogen Fertilizers Produced in Czechoslovakia 10 7. Estimated Production of Fertilizer Nitrogen in Czecho- slovakia, Selected Years, 1930-5~+ 10 Approved For Release~kjCII~~DP79-01093A000400180001-5 Approved For Release 1999/09/02 CIA ~9~~93A000400180001-5 . Page 8. Estimated Production of Ammonium Nitrate and Ammonium Sulfate Fertilizers from Synthetic Ammonia in Czecho- slovakia, 1953 11 9. Estimated Production of Synthetic Nitrogen Fertilizer Plants in Czechosl+~vakia, 1953 and 1954 12 10. Total Estimated Production of All Forms of Fixed Nitrogen in Czechoslovakia, Selected Years, 1930-54 13 11. Estimated Imports of Nitric Acid by Czechoslovakia, 1951-54 . 14 12. Estimated Imports of Nitrogen?Fertilizers by Czecho- slovakia, 1950-53 15 13. Estimated Production, Consumption, and Net Trade in Synthetic Ammonia, Nitric Acid, and Nitrogen Fertilizers by Czechoslovakia, 1953 16 14. Estimated Production, Consumption, and Net Trade in Nitrogen Fertilizers by Czechoslovakia, Selected Years, 1935-54 16 15. Planned Production, Consumption, and Net Trade in Nitrogen Fertilizers in Czechoslovakia, 1848-53 17 16. Estimated Consumption of Synthetic Ammonia in Czechoslovakia, 1953 17. .Estimated Consumption of Nitric Acid in Czecho- slovakia, 1953 ? 19 20 18. Input Requirements for the Manufacture of Synthetic Ammonia in Czechoslovakia, 1953 22 19. Input Requirements for the Manufacture of Nitric Acid in Czechoslovakia, 1953 23 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 ?CIA-RDP79- 1093A000400180001-5 Ftn~ emu . y..... 20. Input Requirements for the Manufacture of Ammonium Nitrate in Czechoslovakia, 1953 24 21. Input Requirements for the Manufacture of Ammonium Sulfate from Synthetic Ammonia in. Czechoslovakia, 1953 25 22. Input Requirements for the Manufacture of Ammonium Sulfate from Byproduct Coke Ovens in Czechoslovakia, 1953 26 23. Input Requirements for the Manufacture of Calcium Cyanamide in Czechoslovakia, 1953 . Following page Fixed Nitrogen Industry: General Process and Use Relationship ~+6 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/0~~~~,~~F~~p1093A000400180001-5 L CIA~RR PR-~+9 (ORR Project 22.1.x+) THE FIXED NITROGEN INDUSTRY IN CZECHOSLOVAKIA~- Summary The purpose of this report is to present an analysis of the fixed. nitrogen industry in Czechoslovakia and to arrive at firm estimates of supplies, consumption, input requirements, capabilities, vulner- abilities, and intentions. As considered in this report, the fixed nitrogen industry is that which produced synthetic ammonia, nitric acid, and nitrogen fertilizers. The nature of the industry ~.ri Czechoslovakia places certain limitations on the scope of the report.. Because of the virtual absence of stock- piling and the relatively minor volume of trade, the analysis of sup- plies is largely confined to production. Because of the industry characteristic of reprocessing some products to produce others, the input study consists of a number of individual input studies, one for each commodity. The basic product of the fixed nitrogen industry in Czechoslovakia is ammonia. A greater part of the industrially applicable forms of fixed nitrogen,. nitric acid and nitrogen fertilizers, is derived from that product. The remainder is supplied in the form of nitrogen ferti- lizer derived from calcium cyanamide. Only three plants in Czechoslovakia are known to be producing syn- thetic ammonia in significant quantities. They are the Dusikarny Plant at Marianske Hory (near Moravska Ostrava), the Synthesis Plant at Sem- tin (near Pardubice), and the Spolek Plant at Usti nad Labem. A fourth plant, the Stalin Works at Zaluzi (near Most), may have begun produc- tion during 1953 but will have little effect upon total industry pro- duction until some time in 195+. A fifth plant, which does not produce synthetic ammonia, is known to be producing nitrogen products. The total estimated production of fixed nitrogen in all forms in Czechoslovakia in 1953 was 51,200 metric tons. Of this total, ~- The estimates and conclusions contained in this report represent the best judgment of the responsible analyst as of 15 December 1953? ~~ Tonnages are given in metric tons throughout this report. Approved For Release 1999/~~~~1~~~;01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 32,200 tons were derived from synthetic ammonia, 15,000 tons from byproduct ammonia, and x+,000 tons were contained in calcium cyan- amide . In Czechoslovakia there is no stockpiling of synthetic ammonia, and, except for seasonal requirements, there is no stockpiling of nitric acid. Neither is there any significant trade in synthetic ammonia. Some nitric acid is imported, largely from East Germany, and nitrogen fertilizers in relatively small quantities are imported, almost entirely from Soviet Bloc countries. Because of the absence of stockpiling, the available supply of fixed nitrogen in Czechoslovakia is the sum of production plus im- ports, and, because there are no exports, consumption .equals avail- able supply. The major inputs to the fixed nitrogen industry are electrical energy and coal. Input quantities are of significance only in terms of individual products of the industry. Estimates of input require- ments for those products are given in the body of the report. The production of fixed nitrogen as synthetic ammonia is currently approaching capacity. By mid-195+, however, additional facilities should be available. Although nitric acid and nitrogen fertilizers are .imported, there appears to be no serious shortage of nitrogen com- pounds. In peacetime the major supply of synthetic ammonia is required in the production of nitric acid, nitrogen fertilizers, and industrial explosives. During a war, .nitrogen products based on. ammonia are indispensable. The same ammonium nitrate used as a fertilizer in peace- time becomes a major component of military explosives in wartime. Furthermore; ammonia or concentrated nitric acid is required in the manufacture of virtually all nonatomic military explosives, and con- centrated nitric acid is one of the most desirable oxidizers for special rocket and guided missile fuels. The industry is self-sufficient as far as raw materials are con- cerned and consequently is not vulnerable to economic warfare, but because of the small number of plants producing nitrogen products and the dependence of those plants on electrical energy and pure synthesis gas the industry is vulnerable to air attack and sabotage. S-E -C -R-E -T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release.1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E-C-R-E-T Current information indicates that agricultural requirements for fixed nitrogen in Czechoslovakia are still being emphasized. A posi- tive indication of a drastically increased armaments program would be an increasing emphasis on the production of nitric acid and, in par- ticular, concentrated nitric acid. This shift in emphasis would be accompanied by a decline in the production and availability of nitro- gen fertilizers, particularly nitrate compounds. To date there has been no clear indication that either situation is developing. I. History and Organization of the Industry. .Following World War I there was rapid worldwide expansion in the production of synthetic ammonia, and several commercially adaptable modifications of the original Faber-Bosch process were developed. The three plants known to be producing synthetic ammonia in Czecho- slovakia at the present time were established during the period from 1928 to 1932. Since World War II, detailed plans have been made to establish 2 new plants and to enlarge the original 3. The probable present status of these plants is considered in Appendix A. Nationalized industry in Czechoslovakia has passed through several organizational stages since 1945. In 1949 "the chemical plants were classified in production branches, regionally divided and combined into national enterprises, which in turn were subordi- nated to the respective industrial section of the Ministry of Indus- tries." l~~ Each of these original enterprises contained several groups, each composed of 2 to 10 plants. The original Synthetic Enterprise controlled 39 plants, but by July 1949 it had been decided to organize certain plants as independent enterprises. 2~ The trend has continued, and it appears that today all the major plants operate independently. In 1951 the Ministry of the Chemical Industry was composed of eight main administrations grouped, in a general way, according to the type of chemicals produced. There were Main Administrations of Fuel, Inorganic Chemistry, Synthetic Fibers, and the like.. At that time ~ Footnote references in arabic numerals are to sources listed in Appendix E. S-E-C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E-C-R-E-T each of the three known producers of synthetic ammonia was a member of a different main administration. 3/ Recent reports indicate that, since 1951, changes have been made in the organization. The new main adrriini.strations are known by numbers, there is a slightly different grouping of the national enterprises under these main administrations, and a separate main administration (VIII now controls all warehouses under the Ministry of the Chemical Industry. ~+~ The three synthetic ammonia plants known to be in production in 1953 are in different main administrations under the Ministry of the Chemical Industry. The administrative organization of these plants in Czechoslovakia in 1952 is given in Table 1. Administrative Organization of Synthetic Ammonia Plants in Czechoslovakia 1952 5/ Administration of the Ministry Plant Location of the Chemical Indust Dusikarny Marianske Hory Main Administration VI Synthetia Semtin Main Administration I Spolek Usti nad Labem Main Administration IV II. Supplies. A. Production. 1. Synthetic Ammonia. The production of synthetic ammonia in Czechoslovakia has been limited,- to date, by the capacity of the established plants. It is estimated that the most significant recent increase in the produc- tion of synthetic ammonia took place between 1949 and 1952, when the largest plant was partially rebuilt and expanded. Anew plant may - ~ - S-E-C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S -E -C -R -E -T have started production during 1953, but significant new production was not anticipated until 1954. The production plans for 1947, and probably 1948, were overfulf filled. Inf ormation available concerning the production of nitrogen fertilizer indicates that more enthusiastic plans for later years have not been met. In particular, the greatly increased 1953 plan for nitrogen fertilizer appears to have been too ambitious, considering the synthetic ammonia known to be available. Estimated production of synthetic ammonia in Czechoslovakia for selected years from 1930 through 1954 is given in Table 2. Estimated Production of Synthetic Ammonia in Czechoslovakia Selected Years, 1930-54 a/ 6/ Metric Tons Production Probable Range Year Synthetic Ammonia Nitrogen Content of Production (Synthetic Ammonia) 1930 13,900 11,500 11,000 to 14,500 1931 12,200 10,000 11,000 to 14,500 1932 14,100 12,000 13,000 to 16,000 1937 lg,4oo 16,000 17,000 to 20,000 1938 20,600 17,000 18,000 to 21,000 1942 29,400 24,200 26,000 to 32,000 1847 7/ 26,000 21,400 21,500 to 29,000 1848 27,700 22,800 26,000 to 29,000 1849 29,800 24,600 28,000 to 33,000 1950 7/ 32,900 27,100 30,000 to 34,000 1951 36,200 29,800 32,000 to 38,000 1952 38,500 31,700 34,000 to 40,000 X953 39,100 32,200 35,000 to 40,000 1954 61,400 50,400 49,000 to 75,000 a. For the methodology used in developing this table, see Appendix C. No new synthetic ammonia plants are known to have begun production since 1932, but two of the original plants have been S-E-C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S -E -C -R-E -T enlarged. The estimated capacity (not actual production) of the 3 plants in production during 1953 is about 42,000 tons of ammonia per year. Tf the capacity of the new Stalin Works is added, the total estimated capacity will be from 57,000 to 77,000 tons in 1954. Current production estimates for synthetic ammonia plants in C2~choslovakia are given in Table 3. Table 3 Estimated Production of Synthetic Ammonia Plants in Czechoslovakia X1953 and 1954 Plant Location 1953 1954. Dusikarny Nia,rianske Hory 26,700 26,700 Synthesia Semtin 9,700 10,000 Spolek Usti nod Labem 2,700 2,700 Stalin Works Zaluzi 22,000 2. Nitric Acid. Nitric acid is produced in both dilute and concentrated forms. The dilute acid averages 60 percent pure nitric acid, and the concentrated acid averages from 96 to 99 percent pure. In arriving at estimates of production and capacity, all nitric acid, both dilute and concentrated, is converted to a basis of 100 per- cent nitric acid. The three plants known to be currently producing syn- thetic ammonia, Dusikarny, Synthesia, a,nd Spolek, are also producing nitric acid. The fourth synthetic ammonia, plant, the Stalin Works, is expected to reach large-scale production of synthetic ammonia in 1954, but probably will not produce nitric acid. S -E -C -R-E -T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S -E -C -R-E -T Table ~+ gives the estimated production of nitric acid in Czechoslovakia as determined from the estimated annual production of individual plants. Table ~+ Estimated Production of Nitric Acid in Czechoslovakia Selected Years, 1930-54 a/ Year Production Probable Range of Production 1930 15,000 11,000 to 15,000 1937 33,300 25,000 to 35,000 1938 36,300 30,000 to 37,000 1842 63,400 60,000 to 72,000 1947 32,000 28,000 to 35,000 1948 37,500 35,000 to 40,000 1949 40,700 36,000 to 44,000 1950 b/ 42,300 37,000 to 45,000 1951 b/ 43,500 37,500 to 46,000 1952 b/ 45,200 41,000 to 48,000 1953 b/ 46,500 42,000 to 49,000 1954 b/ 46,500 42,000 to 49,000 a. Production figures are on the basis of 100 percent nitric acid. For the methodology used in developing this table, see Appendix C.. b. For this year, 4,000 to 5,000 tons of concentrated nitric acid are included. The remainder is produced with an average 60 percent pure acid content. In terms of potential rather than actual production, the 3 plants currently producing nitric acid have an estimated total capacity of 78,000 tons of 100 percent nitric acid. Of this total the greater part is dilute acid capacity. The only significant concentrated nitric acid capacity, 8,500 tons, is that of the Synthesis Plant at Semtin. The Spolek Plant at Usti nad Labem undoubtedly produces small quantities of concentrated nitric acid for its dye and intermediate chemical products, but neither capacity -7- S -E -C -R-E -T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E -C -R-E -T nor production figures for concentrated nitric acid ai=e known. It is believed that the Dusikarny Plant at Marianske $ory, the largest nitric acid producer, has no capacity for concentrated acid produc- tion. Neither the Stalin Works at Zaluzi nor the new Nitrogen Products Plant at Lovosice has any capacity for-the production of nitric acid, either dilute or concentrated. The latter plant, how- ever, can be expected to install nitric acid production facilities within the next few years. Actual production is substantially lower than production capacity.- Current production estimates for nitric acid plants in Czechoslovakia are given in Table 5. Estimated Production of Nitric Acid Plants in Czechoslovakia 1953 and 195+ a/ Metric Tons Plant Location 1953 195+ Dusikarny Marianske Rory 28,000 28,000 Synthesia Semtin 16,500 b / 16,500 b / Spolek Usti nad Labem 2,000 2,000 a. ~'roduction f~ res are on the basis of 100 per- cent nitric acid. b. Production f~.gure includes about 5,000 tons of concentrated nitric acid. 3. Nitrogen Fertilizers. Several types of nitrogen fertilizer are produced in Czechoslovakia. To obtain-both a common basis for the .comparison of production and a meaningful total production figure, all ferti- lizer production estimates in this report will be expressed in terms of nitrogen content S E-C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E-C-R-E-T The average nitrogen content of all nitrogen fertilizers produced in Czechoslovakia up to 1939 was 18.5 percent. Currently, the average nitrogen content is believed to be slightly higher -- about 19 percent. Production estimates can be made for three different categories of nitrogen fertilizers as follows: a. Nitrogen FertiliZe.rs from Synthetic Ammonia. These products are the various mixed fertilizers produced from synthetic ammonia. The nitrogen is actually supplied by nitric acid and~or ammonia, depending on the product. The two major products in this group are ammonium nitrate and ammonium sulfate. b. Byproduct Ammonium Sulfate. This fertilizer is produced from the ammonia liquor recovered at coke plants. Thus it is not a product of the synthetic ammonia industry. -The total nitrogen content of this fertilizer pro- duced during 1953 amounts to about 40 percent of the total fertilizer nitrogen produced during that year. c. Calcium Cyanamide. One plant at Sokolov (German name -- Falkenau) pro- duces all the cyanamide fertilizer in Czechoslovakia. The total nitrogen content of this fertilizer produced during 1953 amounts to about l0 percent of the total fertilizes nitrogen produced during that year. The average nitrogen content of the ma,~or nitrogen fertilizers consumed in Czechoslovakia is given in summary form in Table 6.* These percentages can be used to calculate the production of nitrogen fertilizers in Czechoslovakia from the total nitrogen estimates of Table 7.~ Table 8 gives the estimated quantities of ammonium nitrate and ammonium sulfate fertilizers produced from synthetic am- monia in Czechoslovakia during 1953? ~ Table7 follows on p. 10. ~ Table 7 follows on p. 10. 8 11 ~ follows on p. Table . -9 S E-C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Table 6 Nitrogen Content of the Ma,~or Nitrogen Fertilizers Produced in Czechoslovakia Fertil~.zer Nitrogen Content (Percent) Ammonium Nitrate 38.00 AuIInonium Sulfate 20 , 6 Ammonium Sulfate-Nitrate Mixture 26.0 Calcium Cyanamide 21.0. Lime Ammonium Nitrate a/ 15.5 Nitrophos b/ 15.5 a. Also known as Ostrava saltpeter, Ostrava nitrate, or Kalkammon saltpeter. Imported lime-ammonium ni- trate normally contains about 20.5 percent nitrogen. b. A mixture of ammonium nitrate and ground phos- phate rock which contains 16 to 18 percent phosphoric anhydride. Table 7 Estimated Production of Fertilizer. Nitrogen in Czechoslovakia Selected Years, 1930-54 a/ ~ 9/ Synthetic Byproduct Ammonium Calcium Year Ammonia Sulfate anamide .Total 1930 7,000 5,000 6,300 18,300 1935 l0 10,500 4,900 x+,300 19,700 1936 lo/ 8,600 6,400 5,000 20,000 1937 10/ 10,100 8,230 5,300 23,630 1938 l0 9,900 8,30? 5,5~ 23,700 1942 DT.A. N.A, N.A. 15,000 1947 12,500 7,500 x+,500 24 500 11/ 1948 15,000 8,000 5,000 , 28,000 '-'- 1949 16,000 10,000 5,000 31,000 12 Footnote for Table 7 follows on p. 11. - 10 - S-E -C -R-E -T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E-C-R-E-T Table 7 Estimated Production of Fertilizer Nitrogen in Czechoslovakia Selected Years, 1930-54 a~ 9/ (Continued) Year Synthetic Ammonia Byproduct Ammonium Sulfate Calcium Cyanamide Total 1950 16,500 12,-000 4,500 33,000 ~ 1951 17.,ooa 13,000 4,000 34,000 x.952 17,000 14,000 4,000 35,000 1953 19,000 15,000 4,000 38,000 1954 37,000 15,000 4,000 56,000 a. Production figures refer to the total nitrogen content only. Except for 1930, production figures through 1938 are reported figures and are considered accurate. Later figures are subject to comparatively large error. The estimated range of production for 1953 is 33,000 to 39,000 tons. For the methodology used in developing this table, see Appendix C. Table 8 Estimated Production of Ammonium Nitrate and Ammonium Sulfate Fertilizers from Synthetic Ammonia in Czechoslovakia 1953 J ? Metric Tons Nitrogen Probable Range of Estimate Fertilizer Lontent Production (Nitrogen Content) Ammonium Nitrate b~ 11,000 29,000 9,000 to 12,000 Ammonium Sulfate 5,500 27,000 4,000 to 7,000 Other Nitrates 2,500 N.,A. 1,500 to 3,500 a?. For the methodology used in developing this table, see Appendix 0. b. These figures do not include excess ammonium nitrate produced by the Synthesia Plant at Semtin, which is consumed in explosives. Probably 5,000 tons of ammonium nitrate are available at the Synthesia Plant for production of explosives. S-E-C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E-C-R-E-T .The estimated production of synthetic nitrogen fertilizers from synthetic ammonia is summarized on a plant basis in Table 9. Table g Estimated Production of Synthetic Nitrogen Fertilizer Plants in Czechoslovakia 7-953 and 195+ a,/ Plant Location 1953 195+ Dusikarny Marianske Hory 17,000 17,000 Synthetic Semtin 2,000 2,000 Nitrogen Products Lovosice b~ Negligible 18,000 a. The plant producing calcium cyanamide and coke plants recovering byproduct ammonium sulfate are not included. Production figures refer to total nitrogen content only. b. See Appendix A. 4. All Forms of Fixed Nitrogen? In Czechoslovakia, fixed nitrogen is produced in three different forms: synthetic ammonia, byproduct ammonium sulfate from coke plants, and calcium cyanamide. The total production .of all forms of fixed nitrogen in Czechoslovakia for several years is summarized in Table 10.E B. Stockpiling. Although there is no specific information concerning the stockpiling policy in Czechoslovakia, it is almost certain t}~at neither synthetic ammonia nor nitric acid is stockpiled at present. There are probably the normal industrial stocks of 1 to 3 months' supply. of nitric acid. An economy mobilized for war requires such Table 10 follows. on. p. 13. S-~ -C -1~-E -T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E -C -R-E -T Table 10 Total Estimated Production of All Forms of Fixed Nitrogen in Czechoslovakia Selected Years, 1930-54 a~ Year Synthetic Ammonia Byproduct Ammonium Sulfate Calcium Cyanamide Total 1930 11,500 5,000 6,300 22,800 1937 16,000 8,230 5,300 29,530 1938 17,000 8,300 5,500 30,800 1947 21,400 7,.500 x+,500 33,400 1948 22,800 8,000 5,000 35,800 1949 24,600 lo,oo0 5,000 39,600 1950 27,100 12,000 4,500 43,600 1951 29,800 13,000 4,000 46,800 1952 31,700 14,000 4,000 49,700 1953 32,200 15,000 4,000 51,200 1954 50,400 15,000 4,000 6g,4oo a. Production figures refer to the total nitrogen content only and are taken from Table 2, p. 5 and Table 7, p. lo. large quantities of nitric acid and ammonia that prohibitive numbers of special pressure vessels and noncorrosive containers would be needed to store significant quantities of these commodities. On the other hand, the nitrogen fertilizer industry is nor- mally seasonal, and storage facilities are provided at producing plants for the storage of several months' production. A practical method of stockpiling nitrogen would be that of stockpiling finished or Semifinished products such as filled munitions, explosives, and ammonium nitrate. Special care i~ needed to store pure ammonium nitrate, which is deliquescent. In synthetic ammonia there ie no significant trade involving Czechoslovakia. There is trade, however, in other nitrogen products, S-E-C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For .Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E-C-R-E-T including nitric acid, fertilizers, and intermediates for dyes and special chemicals. During recent years, Czechoslovakia has imported nitric acid. Nearly all of it has come from East Germany, but there have been occasional shipments from Hungary. There is no information concern- ing trade with the USSR. The C$echs had intended to increase the production of nitric acid suff iciently by 195+ to dispense with imports. If this plan was based on expected production from a new plant, it may not be realized by 195+. Estimated imports of nitric 'acid by Czechoslovakia from 1951 through 195+ are given in Table 11. Estimated Imports of Nitric Acid by Czechoslovakia . 1951-5~+ J d3/ Year Metric Tons 1951 3,000 1952 1,500 1953 2,000 195+ l,ooo b/ a, Practical]~y all imports are from East Germany. Import figures are on the basis of 100 percent .nitric acid. b. It was planned to discontinue imports of nitric acid in 195+. It is doubtful now that a new plant will start. production by that time, as was originally planned. Czechoslovakia has been a net .importer of nitrogen ferti- lizers every year. If expansion plans materialize on schedule, large imports should not be required after 1953? Before World War II, imports averaged about 2,000 tons of nitrogen. About 75 percent of this nitrogen was in the form of Chilean nitrate, and the remaining 25 percent was in the form of calcium cyanamide. -1~+- S-E-C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E-C-R-E-T Since World War II the imports have included ammonium ni- trate and ammonium sulfate from the USSR, lime-arrunonium nitrate from Austria, and ammonium sulfate and lime-ammonium nitrate from East Germany. France supplied some unspecified nitrogen ferti- lizers during 1950 and 1951. Estimated imports of nitrogen ferti- lizers by Czechoslovakia from 1950 through 1953 are given in Table 12. There have been rare and insignificant exports of nitrogen fertilizers, apparently on an individual contract basis. Estimated Imports of Nitrogen Fertilizers by Czechoslovakia 1950-53 1?+/ Exporter 1950 1951 1952 1953 Soviet Bloc 3,000 a/ x+,000 8,500 8,000 West 7,900 6,300 Austria 7,500 6,100 France x+00 200 a. Import figures refer to total nitrogen content only. D. Availability. . As there is no trade in synthetic ammonia and there is not believed to be any stockpiling, consumption and availability are equivalent to the national production. Some nitric acid is imported at present, but it is planned to increase production in order to dispense with such imports. Some nitrogen fertilizers are also imported, but new plant facilities should help in overcoming the shortage during 195+? S-E-C -R-E -T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E-C-R-E-T The estimated availability of synthetic ammonia, nitric acid, and nitrogen fertilizers in Czechoslovakia during; 1953 is given in Table 13. Table 13 Estimated Production, Consumption, and Net Trade in Synthetic Ammonia, Nitric Acid, and Nitrogen Fertilizers by Czechoslovakia 1953 Commodity Production Consumption Net Trade Synthetic Ammonia 39,100 39,100 0 Nitric Acid a/ 46,500 48,500 + 2,000 b/ Nitrogen Fertilizers c/ 38,000 46,000 + 8,000 a. Figures are on the basis of 100 percent nitric acid. b. Plus (+) indicates ne-t imports. c. Figures refer to the total nitrogen content only. Tables 14 and 15~ are presented for comparison. The esti- mated availability of nitrogen fertilizers in Czechoslovakia over several years is summarized in Table 14. .Table 14 Estimated Production, Consumption, and Net Trade in Nitrogen Fertilizers by Czechoslovakia Selected Years, 1935-54 a/~' Year Production b/ Consumption -Net Trade 1935 19,700 21,880 + 2,180 15/ c/ 1936 20,000 22,110 + 2,110 15/ - 1937 23,630 24,830 + 1,20o i5/ Table 15 follows on p. 17. Footnotes for Table 14 follow on p. 17. - 16 - S-E-C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E-C-R-E-T Table 14 Estimated Production, Consumption, and Net Trade in Nitrogen Fertilizers by Czechoslovakia Selected Years, 1935-54 a/ (Continued) Year Production ~ / Consumption Net Trade 1938 23,700 24,700 + 1,000 15/ 1942 15,000 15,000 0 1847 24,500 28,500 + x+,000 1948 28,000 33,000 + 5,000 a/ lg4g 31,000 36,000 + 5,000 a/ 1950 33,000 43,900 +10,900 e/ 1851 34,000 44,300 +lo,Sob e/ 1952 35,000 43,500 + 8,500 e/ ' 1953 38,000 46,000 + $,000 e/ 1954 56,000 56,000 0 a. Figures refer to the total nitrogen content only. b. Production figures are taken from Table 17, p. 10. c. Plus (+) indicates-net imports. d. Plan figure is taken from Table 15, p. 17. e. Import figure is taken from Table 12, p. 15. Planned Production, Consumption, and Net Trade in Nitrogen Fertilizers by Czechoslovakia 1848-53 ~ 16 Metric Tons Year Production Consumption Net Trade 1848 28,270 33,270 + 5,0.00 b / ig4g 29,681 34,681 + 5,000 Footnotes for Table 15 follow on p. 18. - 17 - S-E -C R-E -T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E -C -R-E -T Table 15 Flanned Production, Consumption, and Net Trade in Nitrogen Fertilizers by Czechoslovakia 1948-53 a/ 16 (Continued Metric Tons Year Production Consumption Net Trade 1950 37,516 1+0,016 + 2,500 1951 39,595 1+2,095 + 2,500 1952 41,191 1+3,681 + 2,500 1953 ~/ 1+2,930 1+5,1+30 + 2,500 a. Figures refer to the total nitrogen content only. b. Plus (+) indicates net imports. . c. In 1951 the .planned production of nitrogen fertilizers for.1953 was increased by 50 per- . cent to about 64,500 tons. 17/ -Table 15 presents the estimated availability of nitrogen fertilizer in Czechoslovakia for 6 years as anticipated by the Czechs in their Five Year Plan (181+9-53)? Comparison with Table 11+ indicates that this original Plan was entirely feasible. III. Consumption. A.~ Synthetic Ammonia. Synthetic ammonia is primarily consumed directly in the pro- duction of nitric acid and fertilizers. Of the total nitric acid produced from synthetic ammonia, 60 to 70 percent is consumed, in turn, in the production of fertilizers. Most of the. remaining ammonia is used in the chemical, metallurgical, and refrigeration industries. One of the chemical requirements for ammonia is in the production of urea. Urea is used to produce glue for the furniture industry and Other synthetic resins for lacquers and plastics. It had been a dollar import] so provision was made to use 350 tons of ammonia to - 18 - S-E-C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E-C-R-EST produce 500 tons of urea at the Dusikarny Plant during 1951. Plans were also formulated for the production of 5,000 tons of urea per year, beginning in 1952. This production would provide about 1,700 tons for export and would require about 3,500 tons of synthetic ammonia. ~ The 1951 production was undoubtedly achieved, but by mid-1953 there was no confirmation of the larger production. As detailed information concerning all requirements for syn- thetic ammonia is lacking, two very general categories, i-n addition to agriculture., will be considered. Table 16 gives the estimated consumption of synthetic ammonia in Czechoslovakia far 1953 by broad categories of use. Table 16 Estimated Consumption of Synthetic Ammonia in Czechoslovakia 1953 J Use Consumption (Metric Tons) Percent of Total Nitrogen Fertilizers 23,100 59.0 Explosives (Industrial and Military) ~ 5,000 12.8 Other 11,000 28.2 a. For the methodology used in developing this .table, see Appendix C. b. This requirement includes ammonia consumed in the production of the required nitric acid. B. Nitric Acid. There is not sufficient detailed information to provide a comprehensive nitric acid consumption pattern. Thus the same broad categories as were used in Table 16 will be used in Table 17~- to express the estimated consumption of nitric acid. Table 17 follows on p. 20. S-E-C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E-C-R-E-T- Miscellaneous uses include the manufacture of many chemicals, dyes, and lacquers. A considerable quantity is also consumed in the metallurgical industry. Table 17 Estimated Consumption of Nitric Acid in Czechoslovakia 1953 a~ Use Consumption (Metric Tons ) Percent of Total Nitrogen Fertilizers 32,000 66.0 Explosives (Industrial and Military) 11,000 22.7 Other 5,500 11.3 a. For the methodology used. in developing this table, see Appendix C, b. Consumption figures are on the basis of 100 percent nitric acid. C. Nitrogen Fertilizers. Although ammonium nitrate can readily be diverted to the pro- duction of explosives, it can be assumed for present purposes that all of the available fertilizer nitrogen will be consumed as ferti- lizer. It is estimated that 46,000 tons of nitrogen were consumed as a constituent of fertilizers during 1953? According to a discussion (1948) of the Five Year Plan (1848-53), the Ministry of Agriculture wanted 60,000 tons of nitrogen. It is also reported that 3.02 kilograms of nitrogen were applied to each hectare of agricultural land in Czechoslovakia in both 1937 and 1938. The Plan anticipated the application of 4.40 kilograms per hectare in 1948, 6.06 kilograms in 1953, a,nd 7.00 kilograms in 1954. Eventually 20 kilograms per hectare would be required. 19~ S-E-C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E-C-R-E-T D. All Forms of Fixed Nitrogen. Consumption estimates for synthetic ammonia and nitric acid cover many of those for all forms of fixed nitrogen. It is important to note, however, that of the total fixed nitrogen available in 1953, about 75 percent, or 46,000 tons, was to be consumed as fertilizer. Immediately after World War II the percentage of the total available fixed nitrogen (including imports) consumed by agriculture amounted to about 73 percent. For comparison it can be noted that in the US agricultural consumption of fixed nitrogen during 1947 and 1948 amounted to about 70 percent of the total supply. In Czechoslovakia the remaining fixed nitrogen is consumed by industry in the form of ammonia, nitric acid, and their deriva- tives. Some calcium cyanamide may be used by the chemical industry. IV. Input Requirements. A. Synthetic Ammonia. Power requirements for synthetic ammonia production vary greatly with the process used. Of a total production of 39,100 tons of synthetic ammonia during 1953, it is estimated that about 68 per- cent, or 2,700 tons, was to be produced from coke-oven-gas hydro- gen; about 25 percent, or 9,700 tons, from coke-water-gas hydrogen; and the remaining 7 percent, or 2,700 tons, from electrolytic hydrogen. The electrical-energy required to produce 1 ton of synthetic ,ammonia by the three different processes is as follows 20~: Coke-Oven-Gas Hydrogen 2,200 Coke-Water-Gas I~ydrogen 1,400 Electrolytic Hydrogen 13,300 The raw material requirements (with the exception of elec- trical energy) for the production of 1 ton of synthetic ammonia are similar to all 3 processes. The following requirements are based on the experience of one US producer: 'S-E-C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E-C-R-E-T Nitrogen Cubic Meters 720 to 800 Hydrogen Cubic Meters 2,000 to 2,x+00 Iron Catalyst Grams 135 to 150 'Water Cubic Meters 100 to x+00 Steam (Process) Metric Tons 1.O to 2.0 Calculated from these coefficients, the quantitative input requirements for the manufacture of 39,100 tons of synthetic ammonia in Czechoslovakia during 1953 are given in Table l8. Table 18 Input Requirements for the Manufacture in Czechoslovakia 1953 of Synthetic Ammonia Raw material and power requirements for the production of nitric acid are similar in all installations although large varia- tions actor in the quantities of cooling water and steam required. The raw materials and the electrical energy required for the manu- facture of nitric acid in the USSR will be used as a basis for determining the requirements in Czechoslovakia. 21~ The average consumption coeff icients for the manufacture of 1 ton of nitric acid are as follows: Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E -C-R-E -T Synthetic Ammonia Kilograms 290 to 300 Platinum Catalyst Grams 0.10 to 0.13 Water .(for Cooling) Cubic Meters 80 to 145 Steam Kilograms 145 to 360 Electrical Energy Kilowatt-Hours 210 to 300 Calculated from these coefficients, the quantitative input requirements for the manufacture of 46,500 tons of nitric acid in Czechoslovakia during 1953 are given in Table 19. Table 19 Input Requirements for the Manufacture of Nitric Acid in Czechoslovakia 1953 Input Unit Requirement Synthetic Ammonia Metric Tons 13,500 to 14,000 Platinum Catalyst Kilograms 4.7 to 6.1 Water (for Cooling) Million Cubic Meters 3.7 to 6.8 Steam Metric Tons 6,800 to 16,700 Electrical Energy Million Kilowatt-Hours 9.8 to-14.0 C. Nitrogen Fertilizers. Input requirements will be .calculated for three major ferti- liters produced in Czechoslovakia. These fertilizers accounted for about 94 percent of the synthetic fertilizer nitrogen produced during 1953? 1. Ammonium Nitrate. The average consumption factors for the production of 1 ton of ammonium nitrate are as follows 22~: S E-C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S -E -C -R-E -T Synthetic 9mmonia Kilograms 217 to 220 Nitric Acid (100 Percent) Kilograms 785 to 795 Steam Kilograms 1+00 to 1,000 Water Cubic Meters 20 to 1+0 Electrical Enemy Kilowatt-Hours 15 to 30 Calculated from these coeff icients, the total quanti- tative input requirements for the production of 31+,000 tons of ammonium nitrate in Czechoslovakia during 1953 are given in Table 20. Input Requirements for the Manufacture of Ammonium Nitrate in Czechoslovakia 1953 Input Unit Requirement Synthetic Ammonia Metric Tons 7,1+00 to 7,500 Nitric Acid (100 Percent) Metric Tons 2,500 to 27,000 Steam Metric Tons 13,500 to 31+,000 Water Thousand Cubic Meters 680 to 1,360 Electrical Energy Thousand Kilowatt-Hours 510 to 1,020 2. Ammonium Sulfate. a. Ammonium Sulfate from Synthetic Ammonia. The average consumption factors for the production of 1 ton of ammonium sulfate from synthetic ammonia are as follows 23/: Synthetic Ammonia Kilograms 260 to 280 Sulfuric Acid (F8 to 71 Percent Pure) Kilograms 7>+5 to 765 Water Cubic Meter 1 Electrical Energy Kilowatt-Hours 18 to 20 S-E-C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E-C-R-E-T Calculated from these coefficients, the total quan- titative input requirements for the production of 27,000 tons of ammonium sulfate from synthetic ammonia in Czechoslovakia during 1953 are given in Table 21. Input Re quirements for the Manufacture of Ammonium Sulfate from Synthetic Ammonia in Czechoslovakia 1953 Input Unit Requirement Synthetic Ammonia Metric Tons 7,000 to 7,600 Sulfuric Acid (68 to 71 Percent Pure) ~2etr3c Tons 20,000 to 21,000 Water Cubic Meters 27,000 Electrical Energy Thousand Kilowatt-Hours x-85 to 5~+0 b. Ammonium Sulfate from Byproduct Coke Ovens. The average consumption factors for the production of 1 ton of ammonium sulfate from byproduct coke ovens are as follows 24/: Byproduct Ammonia X100 Percent) Kilograms- 250 to 260 Sulfuric Acid (75 to 78 Percent Pure) Kilograms 96Q to 980 Steam Metric Tons 3 to 6 Water Cubic Meters 6 to 8 Electrical Energy Kilowatt-Hours 25 to 30 Calculated from these coeff icients, the total quan- titative input requirements for the production of 78,000 tons of byproduct ammonium sulfate in Czechoslovakia during 1953 are given in Table 22.E Estimated. ~ Table 22 follows on p. 26. S-E -C -R-E -T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S E-C-R-E-T Table 22 Input Requirements for the Manufacture of. Ammonium Sulfate from Byproduct Coke Ovens in Czechoslovakia 1953 Input Unit Requirement Byproduct .Ammonia (100 Percent) Metric Tons 19,500 to 20,200 Sulfuric Acid (75 to 78 Percent Pure)' Metric Tons 75,000 to 77,000 Steam Thousand Metric Tons 235 to 1+70 Water Thousand Cubic Meters 1+68 to 625 Electrical Energy Million Kilowatt-Hours 1.9 to 2.3 3. Calcium Cyanamide. The requirements for the manufacture of 1 ton of calcium cyanamide are as follows 25~: Calcium Carbide Kilograms 650 to 750 .Nitrogen Cubic Meters 160 to 300 Electrical Energy Kilowatt-Hours 80 to g0 .Calculated from these coefficients, the total quantitative input requirements for the manufacture of 18,000 tons of calcium cyanamide in Czechoslovakia during 1853 are given in Table 23?~ V. Capabilities, Vulnerabilities, and Intentions. A. Capabilities. :The capabilities of Czechoslovakia in the production of fixed nitrogen are important not because of trae tiize of the industry but because the industry supplies raw materials. to several other strategic industries. It is estimated that during 1953 Czechoslovakia produced ~ Estimated. '~ Table 23 follows on p. 27. - 26 - Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E -C'-R-E -T Table 23 Input Requirements for the Manufacture of Calcium Cyanamide in Czechoslovakia 1953 Input Unit Requirement Calcium Carbide Metric Tons 12,500 to 14,500 Nitrogen Million Cubic Meters 3.2 to 5.7 Electrical Enemy Million Kilowatt-Hours 1.5 to 1.7 an estimated 39,100 tons of synthetic ammonia, or a little more than 5 percent of the corresponding estimated production of the USSR. 26~ The nitrogen content of this ammonia is available to the modern and well-organized explosives and munitions industry. Other chemical industries also have strategic uses for this nitrogen. The production of fixed nitrogen as synthetic ammonia is currently approaching capacity. The synthetic ammonia available during 1953 could have provided as much concentrated nitric acid for strategic uses as was available during World War II. The explosives industry of Czechoslovakia could readily use the con- centrated nitric acid to produce additional quantities of. TNT (trini- trotoluene , picric acid, hexogen, and other military explosives. Whatever amount of ammonium nitrate is produced with the remaining nitric acid and ammonia can be allocated to the explosives industry and agriculture as desired. By the end of 1953, additional capacity should be availabl e for the. production of synthetic ammonia and nitrogen fertilizers. A logical development to expect in the near future would be the con- struction of additional nitric acid capacity. S-E -C -R-E -T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S -E -C -R-E -T B. Vulnerabilities. The fixed nitrogen industry of Czechoslovakia is self-sufficient in regard to raw materials and consequently is not vulnerable to economic warfare. Construction of new facilities in Czechoslovakia has been de- layed, however, by the restrictions placed by the West on the export of specially designed equipment. 27~ As a limited number of plants make up the industry, it is vulnerable to air attack. The vulnerability of synthetic nitrogen plants was demonstrated during World War II. Three plants produce nearly all of the nitrogen products of strategic value at present, and 2 more may be in production by 1954. Within the industry the production anal availability of synthetic ammonia is the determining factor in the production of nitric acid and the many end products of military signif icance. The asrnnonia-producing units, in turn, depend upon adequate supplies of pure synthesis gas and electrical enemy. Both of these input items are produced within or near the individual plant. Interrupting the supply of either would stop plant production. In addition, an interruption in the electricity or hydrogen supply at these plants would seriously affect production of synthetic methanol at the Stalin Works and at the Dusikarny Plant as well as production of synthetic fuel at the Stalin Works. Information through 1953 indicates the agricultural require- ments for fixed nitrogen in Czechaslovakia are still being emphasized. Originally, the one important new nitrogen installation planned since World War II was to reserve 50 percent of the nitrogen for the Ministry of National Defense. Since that time, however, the plans have been involved in various degrees of political intrigue, and it now appears that new nitrogen production will be considerably less than originally planned. It is expected that during 1954 the new facilities will pro- duce only ammonia and ammonium sulfate. These products are primarily for agricultural use and are of no direct value to the military estab- lishment. A positive indication of a drastically increased armaments. program would be an increasing emphasis on the production of nitric acid and, in particular, concentrated nitric acid. This shift in emphasis would be accompanied by a decline in the production and -28- S-E-C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S -E -C -R-E -T availability of nitrogen fertilizers, particularly nitrate com- pounds. To date there has been no clear indication that either situation is developing. S -E -C -R-E -T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S -E -C -R-E -T APPENDIX A FIXED NITROGEN PLANTS IN CZECHOSLOVAKIA. 1. Dusikarny Plant. 28/ a. Full Name. Dusikarna Ostravske Chemicke Zavody (Nitrogen Plant of the Ostrava Chemical Works). b. Location. Marianske Hory (near Moravska Ostrava). c. Coordinates. 4g?5o' N - 18?15' E. d. Estimated Annual Capacity (Metric Tons). ~nthetic Ammonia Nitric Acid (100 Percent) 1930 13,500 1930 21,000 1932 18,000 World War IT 48,000 1942 28,000 29/ 1949 50,000 30/ 1953 55,000 Nitrogen Fertilizers (Nitrogen Content) 1849 25,000 e. Estimated Annual Production (Metric Tons). Synthetic Ammonia DTitric Acid (100 Percent) 1950 . 23,000 (22,000 to 25,500) .1950 26,000 (23,000 to 28,000) 1951 25,500 (22,000 to 26,700) 1951 27,000 (23,000 to 28,000) 1952 26,700 (24,300 to 28,000) 1952 28,000 (25,000 to 30,000) 1953 26,700 (24,300 to 28,000) 1953 28,000 (25,000 to 30,000) 1954 26,700 (24,300 to 28,000) 1954 28,000 (25,000 to 30,000) S-E-C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Nitrogen Fertilizers (Nitrogen Content) 1950 15,000 (13,000 to 18,000) 1951 15,500 (13,000 to 18,000) 1952 15,500 (13,000 to 18,000) 1953 17,000 (14,000 to 19,000) 1954 17,000 (14,000 to 19,ac~) f. Process. The ammonia is synthesized by the Claude process, which operates at an elevated pressure of about 1,000 atmospheres and at about 4oo~C. Five Skoda 7-stage compressors were in use in 1948, 2 for ammonia synthesis, 1 for methanol synthesis, and 2 in reserve. The iron oxide cata~,yst was formerly obtained from France, but in 1948 a lower-quality catalyst was being produced at the plant. 31/ Standard processes are used for the production of nitric acid by the oxidation of ammonia and subsequent absorption of the oxides in water. According to one report, the entire installation is of Fauser design, and the product is about EG percent nitric acid. Another report states that a Fauser unit produces acid of 48 to 50 percent strength. Various fertilizer mixtures are produced by standard neutrali- zation processes. g. Comments. The capacity figures as given for ammonia are well documented. It is interesting to note that one. source reports that the first unit was installed during the period from 1928 to 1930 and had a capacity of 7,200 tons of nitrogen and that a second unit was added immediately. Prior to World War II, plans were made to add a third unit as well as to improve efficiency to a capacity of about 23,000 tons of nitrogen. This suggests that any future expansion may be accomplished by adding units of about 7,500 tons of nitrogen annually. The capacity figure for nitric acid in 1949 is firm. There were plans at that time to increase the capacity by adding more absorbers. Considering the over-all activity at the plant, it is estimated that the capacity for nitric acid during 1953 was about S-E -C -R-E -T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E -C -R-E -T 55,000 tons expressed as 100 percent acid. The reported capacity for fertilizer production in terms of nitrogen content is considered firm. Yearly production estimates for 1834 to 1938 were prepared from firm national production reports after making allowances for other forms of fertilizer nitrogen. Since World War II the production estimates have been based on the availability of nitrogen at the plant as well as on the few reports concerning national praduction of nitrogen fertilizers. Most of the fertilizer is produced as compound, or mixed, fertilizer. Ostrava saltpeter (lime-ammonium nitrate), one of the main products, is a mixture of potassium, sodium, calcium, and ammonium nitrates, containing about 15.5 percent nitrogen. Ammonium sulfate-nitrate mix, or compound fertilizer B, contains 26 percent nitrogen. A third fertilizer,. known as Nitrophos, is a mixture of ammonium nitrate and ground phosphate rock containing 15.5 percent nitrogen and 16 to 18 percent phosphoric anhydride. Some ammonium chloride is also mixed with lime for use as a fertilizer. 32/ 2. Synthetia Plant. 33/ a. Full Name. Synthesis Narodni Podnik (Synthesis National Corporation). b. Location. Semtin (near Pardubice). c. Coordinates. 50002' N - 15047' E. d. Estimated Annual Capacity (Metric Tons). Synthetic Ammonia Weak Nitric Acid* 1832 4,200 1949 12,000 1937 -7,000 1g48 10,500 34/ Concentrated Nitric Acid- Ammonium Nitrate 1944 6,000 1848 g,ooo 1848 8,500 35/ -~ Figures are on the basis of 100 percent nitric acid. -33- S-E-C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02: CIA-RDP79-01093A000400180001-5 S-E-C-R-E-T e. Estimated Annual Production (Metric Tons). Synthetic Ammonia Weak Nitric Acid 1950 7,300 (6,000 to 7,900) 1950 11,000 (g,ooo to 12,000) 1951 8,100 (6,700 to 8,500) 1951 11,000 (9,000 to 12,000) 1952 8,100 (7,300 to 9,700) 1852 11,500 ((10,000 to 12,000) 1953 9,700 (7,900 to 10,100) 1953 11,500 (10,000 to 12,000) 195+ 10,000 (7,g00 to 10,100) 195+ 11,500 (10,000 to 12,000) Concentrated Nitric Acids .Ammonium Nitrate 1950 ~+ 000 ' 1950 9,000 (8,000 to 11,000) 1951 ~+ oo0 1951 9,500 (8,000 to 11,000) 1952 4,000 1952 10,000 (9,000 to 11,000) 1953 5,000 1953 10,000 (9,000 to 11,000) 195+ 5,000 195+ 10,500 (g,ooo to 11,000) f. Process. Ammonia is synthesized by the ICI (Imperial Chemical Industries) process. This process is similar to the Haber-Bosch process, using a "promoted" catalyst of iron oxides and operating at 200 to 250 atmos- pheres pressure. The hydrogen is provide d. by coke-water gas, and the nitrogen by a liquid-air installation. Concentrated nitric acid is produced directly by oxidation of ammonia, according to the German Hoko process. 36/ The Synthesia Plant and the plant .formerly known as Explosia are neighboring units of a combine built chiefly for the production of explosives. The construction of the Explosia Plant was begun in 1928, and the synthetic ammonia unit of the Synthesia Plant was com- pleted during the following 2 years. The nitrogen products are uti- lized in peacetime as fertilizer and in the production of specialty chemicals as well as in the production of military and industrial explosives. Figures. are on the basis of 1Q0 percent nitric acid.. ~ This quantity of ammonium nitrate is apportioned among fertilizer and explosives production as required. _3~_ S-E -C-R-E -T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E-C-R-E-T The capacity figures given for weak nitric acid and concen- trated nitric acid are not final. They have not been conf armed, and there is no firm basis for a current capacity estimate for ammonium nitrate. Such capacity is relatively easy to add to, however, and in view of the general expansion activities recently taking place and the availability of raw materials, it is believed -that the ammonium nitrate capacity is current7~y about 12,000 tons annually. In 19118 there were plans to double the production facilities for ammonia and nitric acid. 37/ Such an increase in capacity is entirely possible,. but at this time there is no positive intelligence available to indicate such expansion. Production estimates for ammonium nitrate and weak nitric acid are based on the availability of nitrogen in the form of ammonia and are limited by plant capacity estimates. In this manner a consump- tion pattern for synthetic nitrogen typical of such plants is developed. Until 1951 the 2 products required 70 to 75 percent of .the available nitrogen, the remaining 25 to 30 percent being used for the production of concentrated nitric acid and various other nitrogen compounds. This concentrated nitric acid is in great demand at nearby plants for special nitration processes in the explosives, pharmaceutical, and intermediate chemicals industries. The Synthesia Plant does not produce enough weak nitric acid to cover its own requirements and those of the nearby explosives, pharmaceutical, and plastics plants. During 19+9, about 10,000 tons of weak nitric acid were received from the Dusikarny Plant, and according to the source this rate was only slight7~y above the normal peacetime shipments. 3. Spolek Plant. 38/ a. Full Name. Spolek pro Chemickou a Hutni Vyrobu (Association for Chemical and Metallurgical Production). b. Location. Usti na,d Labem (German name -- Aussig). c. Coordinates. 50?~+2' N - 14?08' E. - 35 - S-E-C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 d. Estimated Annual Capacity Metric Tons). ,Synthetic Ammonia Weak Nitric Acid* 1828 3,400 1928 1,500 1951 2,200 e. Estimated Annual Production (Metric Tons). Synthetic Ammonia Weak Niiric Acid 1950 2,600 (2,200 to 2,700) 1950 1,400 (1,200 to 1,500) 1951 2,600 (2,200 to 2,700) 1951 1,600 (1,500 to 2,000) 1952 2,700 (2,300 to 2,800) 1952 1,800 (1,500 to 2,000) 1953 2,700 (2,300 to 2,800) 1953 2,000 (1,800 to 2,100) 1954 - 2,700 (2,300 to 2,800) 1954 2,000 (1,800 to 2,100) f. .Process. The NEC (Nitrogen Engineering Corporation) process normally employs a promoted catalyst of iron oxide granules operating at 300 to 400 atmospheres pressure and about ~-75oC. Pure hydrogen is pro- duced as a byproduct of the electrolysis of brine solutions, and nitrogen is provided by Linde-Frankl air machines. g. Comments. This plant is the smallest producer of synthetic ammonia in the country and as such consumes a relatively large percentage of its own ammonia and nitric acid in the production of specialty prod- ucts. The plant was the original producer of dyes and fine chemicals in Czechoslovakia. Although the reported production of synthetic ammonia has varied greatly, a sound technical check of production and capacity figures can be made by considering the amount of pure hydrogen avail- able. hydrogen is produced here at the same time as chlorine, sodium hydroxide, and potassium hydroxide by electrolyzing solutions of sodium and potassium chlorides. ~' Figures are on the basis of 100 percent nitric acid. - 36 - S-E-C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E -C -R-E -T On the basis of reliable information, which indicates a produc- tion capacity of 17,000 tons of sodium hydroxide and 5,000 tons of potassium hydroxide, 5.6 million cubic meters of pure hydrogen would be available for ammonia synthesis. 39/ Theoretically, about 2,000 cubic meters of pure hydrogen would be required per ton of ammonia produced. If allowance is made, however, for loss and inefficiency, about 2,200 cubic meters of hydro- gen are actually required to produce 1 ton of ammonia. If 5.6 million cubic meters of hydrogen are available, the maximum production of synthetic ammonia will be about 2,600 to 2,700 tons per year. Increasing electrolytic efficiency or capacity could make more hydrogen available for a slight increase in ammonia production. Since 1950 there has been no evidence of new construction in the electrolytic department. The production of profitable dyes and specialty products has been based largely on the availability of nitric acid, Until 1950, nitric acid capacity was 1,500 tons per year (100 percent basis , in- cluding acid of 36 percent, 1+8 percent, and 80 percent strength. The equipment was in poor condition, and definite plans were made to in- stall new plant facilities for the production of 3,600 tons of nitric acid. This would probably amount to about 2,200 tons on a 100 percent basis, and this is assumed to represent current capacity. The Spolek Plant is not believed to possess capacity for any significant production of concentrated nitric acid. During World War II, Germany obtained about 6,000 tons of.ni:tric acid (98 percent) per year from the Aussiger Verein at Prague, but this- is believed to have been produced at Semtin. ~+. Stalin Works . ~+0/ a. Full Name. Stalinovy Zavody (Stalin Works). b. Location. Zaluzi (near Most). c. Coordinates. 50?34' N - 13?36' E. - 37 - S-E-C-R-E -T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved. For .Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E-C-R-E-T d. Estimated Annual Capacity (Metric Tons). Synthetic Ammonia 28,000 (15,000 to 35,000) e. Estimated Annual Production (Metric Tons). Synthetic Aimnonia 1953 Negligible 1954 22,000 (12,000 to 28,ooa) Specific process and operating conditions are not known. Hydrogen is available from Winkler generators, which also provide the hydrogen for synthetic fuel production. Nitrogen is available from Linde-Frankl air machines, which produce oxygen used in the production of synthetic fuel. g. Comments. The estimates listed above are based solely on actual plans made zn 1g48, as interpreted with the aid of sparse current intelligence. A hydrogenation plant of this type is an ideal location for the syn- thesis of ammonia. .Raw materials, high-pressure equipment, and properly trained personnel are already available. According to a reliable report, designs were prepared dur- ing 1947 for an ammonia unit with an annual capacity of 35,000 to 40,000 tons. Political influence sub sequentlry caused plans to be made for the construction of a plant in the vicinity of Moravska Ostrava with an annual capacity of about 50,000 tons of ammonia. At that time (early 1948) it was decided to erect an ammonia synthesis unit at the Stalin Works to start producing during 1952 at the rate of 15,000 to 20,000 tons annually. Thais plant was well along in the design stage by mid-1948. 41~ No plans were made to utilize the ammonia at the plant. A pipeline to "Usti nod Labem or some undetermined place" was under consideration, which is significant when it is realized that Lovosice - 38 - S-E-C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E-C-R-E-T is ,just south of Usti nad Labem and about 30 kilometers from Most. 42~ A 1952 report states that the new Nitrogen Products Plant at Lovosice is connected by underground pipeline with the Stalin Works.'43/ A later (1953) report indicating that the Nitrogen Products Plant at Lovosice is using the ammonia produced at the Stalin Works confirms the existence of this connecting. pipeline . ~+~+~ There have been reports of efforts by Czechoslovakia to obtain plant and equipment from outside the country. An ammonia synthesis plant was requested from the French firm, Air-Liquide, during 1950 or early 1951. ~+5~ In the spring of 1952 the East German Central Off ice for Research and Technology (ZAFT) received a request #'rom Czecho- slovakia for information concerning a cracking unit to produce a synthesis gas from cokery gas. The annual. capacity of a plant based on such a cracking unit would be 2~+t000 to 28,000 tons of arrnnonia or 20,000 to 23,000 tons of nitrogen. 46~ The plant requested from France was not available, and there is no report of a definite order or of delivery of the cracking unit from East Germany. This equipment could be used at the Stalin Works or to provide additional capacity at the Dusikarny Plant at Marianske Hory. It is not known when the plant will (or did) begin production, but no substantial production was expected during 1953? The Nitrogen Products Plant at Lovosice was not expected to be able to start pro- ducing fertilizers until late 1953. 5. Nitrogen Products Plant at Lovosice. ~+7~ a. Location. Lovosice. b. Coordinates. 50031' N - l~+?0~+' E. c. Estimated Annual Capacity. Not available. d. Estimated Annual Production (Metric Tons). Nitrogen Fertilizer (Nitrogen Content) . 1953 Negligible 195+ 18, o00 (11, o0o to 2~+, o00 ) S-E -C -R-E -T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E -C -R-E -T The specific process and equipment to be used are not known. The various processes, however, differ only in details. Most of the fertilizer produced at present is probably ammonium sulfate, but some ammoniated superphosphates may be produced. f. Comments. This is the plant publicly identified as the proposed. Martinov Plant at Hlucin. Construction was stopped at Hlucin in 1950, and the project was abandoned. The site at Lovosice is re- ported not suitable in all respects. ~8~ The nitrogen fertilizer plant is one of a group of plants at Lavosice producing sulfuric acid, superphosphates, and rayon. There are no facilities for the production of a synthesis gas, ammonia, or nitric acid. ~A logical development for the near future would be the installation of equipment for the production of nitric acid. In 19+8, plans were made for the production of synthetic ammonia at the Stalin Works and for the installation of an underground pipeline to transport the ammonia. ~+9~ A 1952 report conf firms the existence of such a pipeline between the Nitrogen Products Plant at Lovosice and the Stalin Works, a distance of about 30 kilometers, 50~ and a 1953 report states that the Nitrogen Products Plant at Lovosice is using the ammonia produced at the Stalin Works. 51~ The estimated production of nitrogen fertilizers is based solely on the estimated availability of synthetic ammonia from the Stalin Works. There is no positive intelligence showing that the fertilizer plant is as large as that originally planned for the Martinov Plant. S-E-C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E-C-R-E-T APPENDIX B BRIEF HISTORY AND TECHNOLOGY OF THE FrXED NI'T'ROGEN INDUSTRY 1. Introduction. As an element in natural and synthesized chemical compounds, nitre- gen is essential to both agrarian and industrial economies. In agri- culture it is utilized primarily for fertilizer. In industry it is essential for the production of explosives, plastics, dyes, pharma- ceuticals, and other industrial chemicals. This report considers only the major nitrogen compounds: synthetic ammonia, nitric acid, acid nitrogen fertilizers. Prior to 1900, chemical, or fixed, nitrogen (as distinct from nitrogen occurring naturally in vegetable and animal matter) was sup- plied by Chilean. saltpeter (sodium nitrate), and ammonia was obtained as a byproduct from the coking of coal. By the turn of the century, increasing nitrogen requirements caused scientists to consider the atmosphere, with its 75 percent nitrogen by weight, as a raw material. Today, elemental nitrogen may be obtained by the fractional distilla- tion of .liquid air. The calcium cyanamide process was the first commercial process to utilize nitrogen from the air. This process, developed in Germany about 1900, was based on the principle that metallic carbides will readily absorb nitrogen gas and form solid cyanamides. Calcium cyanamide so formed can be used as fertilizer. Fuxther treatment of this compound will result in the formation of other nitrogen-bearing compounds. With the advent of low-cost hydroelectric power, interest in an electric arc process was revived, and in 1904 a successful operation was begun in Norway. In this process, air is passed through an electric arc which burns a small fraction of the nitrogen to nitric oxide. The electric arc process and the cyanamide process both re- quire considerable electric energy, as calcium carbide, used in the cyanamide process, is produced in an electric furnace. The direct synthetic ammonia (Haber-Bosch) process, developed in Germany in 1910, provides the most economical method of nitrogen - 41 - S-E -C -R-E -T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E-C-R-E-T fixation by the combination of atmospheric nitrogen with hydrogen to form synthetic gaseous ammonia. This process has now almost entirely replaced the two earlier processes. The cyanamide process is still used as a means of fixing atmospheric nitrogen for fertilizer but not as a producer of ammonia and ammonia salts. The hydrogen required for the Haber-Bosch process may be ob- tained from any of several sources.: (a) electrolytic chlorine cells, (b) electrolytic decomposition of water, (c) semi-water gas from coke, (d) coke-oven gas, (e) natural gas, (f) gas from lignite, or (g) petro- leum refinery gas. The source utilized by any particular plant will depend on the installation and on availability of raw material. Today, synthetic ammonia produced by the Haber-Bosch rocess, or one of its several modifications, provides approximately ~0 percent of the world's production of chemical nitrogen for industrial and agricultural use. 52~ Nitrogen is made available for commercial use in the following forms: (a) aqua ammonia, ammonia in a water solution, for use as liquid fertilizer or as an inexpensive base in a multitude of indus- trial reactions; (b) liquid anhydrous ammonia (under pressure) for use as a refrigerant; and (c) gaseous or liquid ammonia for use in the production of ,industrial organic chemicals and explosives. T.n peacetime the mayor requirements of synthetic ammonia are for the production of nitric acid, nitrogen fertilizers, and commercial explosives. In wartime, nitrogen compounds synthesized from ammonia are indispensable,-and the ammonium nitrate used as fertilizer in peacetime becomes a mayor component of explosives. In addition, am- monia and concentrated. nitric ,acid are required in the manufacture of all conventional (nonatomic) military explosives. Concentrated nitric acid is used ~s an oxidizer for rocket and guided missile petroleum- base fuels. $ydrazine, N2H~, is used as a fuel or fuel igniter in rockets and in the Walther torpedo. ~. Technology.~- a. Synthetic Ammonia. Synthetic ammonia, NH3, is produced by combining atmospheric nitrogen with hydrogen. ~ A chart illustrating the technology of the fixed nitrogen industry fOllOWS p. 1FG. S-E-C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E -C -R-E -T The processes used throughout the world are based almost ex- clusively on the original Haber-Bosch method of bringing pure hydro- gen and nitrogen together under suitable conditions of pressure and temperature in the presence of a positive catalyst and the subsequent recovery of the ammonia produced. The production of synthetic ammonia consists basically of four well-defined steps: (1) production of the hydrogen-nitrogen gas mixture, (2) purif ication of the-gas mixture, (3) compression of the hydrogen-nitrogen mixture and the synthesis of arnrnonia, and (~+) recovery of pure ammonia from the unreacted gases. The production and purification of the synthesis gas (3 parts hydro- gen and 1 part nitrogen) account _f or approximately 75 percent of the manufacturing cost of synthetic ammonia. Nitrogen from the atmosphere is supplied by 1 of 3 methods: (1) air can be liquefied under pressure, and the pure nitrogen recovered by distillation; (2) air can be intro- duced into the gas generator and burned to remove the oxygen; or (3) steam and air can be blown continuously through an incandescent bed, resulting in the formation of a gas containing nitrogen, hydrogen, and carbon monoxide. There are many technical differences among the dozen or so commercial processes in use throughout the world, but the major dif - ference~ one which can be used to identify a particular process, lies in the operating pressure used in the synthesis. Typical pressures range from slightly below 100 atmospheres in the Mont Cenis process to slightly over 1,000 atmospheres in the Claude process. The operating temperatures range from x+00?C to 650?C. Regardless of the specif is source of nitrogen and hydrogen utilized, the equipment must be of sufficiently rugged construction to withstand the high pressures and temperatures required and must be lined with special corrosion-resis- tant alloys. The conversion of the gas mixture to ammonia is realized in useful percentages only in the presence of a catalyst (material which promotes a desired chemical reaction without itself becoming part of the final product). Arty' one of several catalysts may be employed, depending upon the particular operating temperature and pressure. Maintenance of the catalyst constitutes a technical problem of some magnitude, for it may be easily "poisoned" (activity reduced). by the presence of foreign material (especially sulfur) in the reactive gas mixture. The variables of temperature, pressure, and catalyst com- bine to determine the single-pass degree of conversion of the gas mixture into synthetic ammonia. S-E-C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E-C-R-E-T b. Nitric Acid. Nitric acid, HN03, is normally produced in two grades, weak and concentrated. The weak nitric acid is a water solution with an ,acid content of 40 to 65 percent. Concentrated nitric acid is acid which is 96 to 99 percent pure. :The earliest method used commercially to produce nitric acid involved the treatment of sodium nitrate with sulfuric acid in cast iron retorts. The residue 3n the retort .after the distillation period contains sodium bisulfate and excess sulfuric acid. This residue, called niter cake, is a raw material in the manufacture of hydro- ch_loric acid. Another method of producing nitric oxide and, in turn, nitric acid is the electric arc process, one which is not currently in general use. Most nitric acid is made by the oxidation of ammonia. Al- though different installations may vary somewhat in equipment design and operating conditions, the basic procf;ss involves the following steps: (1) ammonia is oxidized to nitric: oxide by passing a mixture of ammonia gas and air, or air enriched with oxygen, through a con- verter, usually employing a platinum-rhodium gauze catalyst, at about 750oC; and (2) the resulting nitric oxide is cooled and further oxi- dized to nitrogen dioxide, which is absorbed in water to form a weak nitric acid solution... If ammonia oxidation is carried out at atmospheric pressure, a nitric acid of about 40 to 55 percent strength is obtained. If it is carried out at pressures up to lOd pounds per square inch, the product contains from 60 to 65 percent nitric acid. Concentrated nitric acid can then be produced in two ways: (1) the weak nitric acid is mixed with sulfuric acid in a retort and distilled to produce a concentrated nitric acid of 99 percent strength; or (2) the ammonia oxidation process, as used to produce weak nitric acid from nitrogen dioxide, is further employed to polymerize the nitrogen dioxide to nitrogen tetraoxide. TYiis liquid nitrogen tetra- oxide is then heated under high pressure (autoclaving) with weak nitric acid and gaseous oxygen to produce concentrated nitric acid up to 99- percent strength. This process is known as the Fauser process. S-E-C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E -C -R-E -T c. Nitrogen Fertilizers. Principal fertilizer constituents-containing nitrogen are as follows: nitrates of ammonium, sodium, calcium, and potassium; ammonium salts such as sulfate, phosphate, chloride, and nitrate; ammonia for ammoniating superphosphates;calcium cyanamide; and synthetic urea. Each compound can be used separately or as a com- ponent of a mixed fertilizer. The production processes for several of the major tonnage items will be discussed here. Small quantities of certain of these products are recovered as byproducts of other manufacturing processes. Most of-such production, however, is pro- vided by the chemical reactions of ammonia or nitric acid with various inorganic compounds. This type of production must be carried out in heavy, but comparatively simple, equipment.. Ammonium nitrate solution is produced by reacting ammonia with dilute nitric acid (about ~+0 percent pure). The water is evaporated, leaving the commercial product in crystalline form. Ammonium nitrate tends to absorb moisture from the atmosphere, and it has been necessary to devise methods for granulating and coating the salt to keep it dry and free flowing. Pelleting, by liquefying and spraying into a cooling chamber tta make small, solid balls with a hard outer surface, is one method of obtaining the desired proper- ties, Large tonnages of sodium nitrate are made by reacting soda ash from the ammonia-soda, or Solvay, proces"s with nitric acid from ammonia oxidatio~i. End use as a fertilizer or as an explosive com- ponent is determined by grain size and purity of the product. The smaller grain sizes are used for gunpower manufacture. Ammonium sulfate may be produced by three commercial methods: (1) ammonia solution recovered from coke oven byproducts is reacted with sulfuric acid; (2) synthetic ammonia is reacted with sulfuric .acid, yielding a very pure product when recovered by crystallizing and centrifuging; and (3) ammonium carbonate is reacted with finely ground gypsum (hydrated calcium sulfate) forming insoluble calcium carbonate and dissolved ammonium sulfate, the two salts are separated by filtration, the ammonium sulfate is crystallized upon evaporation, and the crystals are then centrifuged and further dried in a rotary dryer. S E-C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E -C-R-E-T The economical production of ammonia by the Haber-Bosch process has made practical use of ammoniated superphosphates as fertilizers, A strong ammonia solution (40 to 80 percent ammonia) is sprayed onto a charge. of superphosphates in a rotating mixer. The, action of the mixer constantly exposes new surfaces to the ammonia. In this process any residual sulfuric acid in the super- phosphate which would cause rotting of the shipping bags is neutra- lized. Calcium cyanamide, CaCN2, formerly the intermediate in the production of ammonia, is widely used as a fertilizer or as an ingredient in mixed fertilizers. Calcium cyanamide is formed when nitrogen gas is brought into contact with finely ground calcium carbide in a cylindrical oven at a, temperature up to about 1,000oC. When the reaction is completed, after 40 to 60 hours, the mass is cooled and pulverized. Water is added to decompose any free calcium carbide and to hydrate the lime. The addition of oil diminishes dustiness. The black powder remaining contains about 60 percent calcium cyanamide and about 22 percent fixed nitrogen. It is used as an ingredient in mixed fertilizer. ' Synthetic urea, NH2CONH2, can be produced commercially by reacting carbon dioxide with calcium cyanamide in water and then hydrolyzing the free .cyanamide so formed with acid. It may also be produced by the indirect dehydration of the intermediate, ammonia carbaxnate; formed by the reaction of excess ammonia and carbon dioxide under high pressure. Urea fertilizers contain more fixed nitrogen (in excess of 40 percent) than any other fertilizer. In addition, urea has an important application in the- manufacture of plastics and resins (urea.-formaldehyde type). - ~+6 - Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 o ++ d N~ N ~y O( ~ Li W Z ~ v X m c ~ m C7 -~ ~; ~ ~~ ~~ ~ ,~" -~ ~ N ~ ~ ~ C U U V d ~ C ++ ~ to ~ ~ . ~ ~ A ~~ ~ ~ ~ O ~ ~ Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S E-C-R-E-T APPENDIX C METHODOLOGY 1. Production. a. Synthetic Ammonia, Table 2. There are available reliable statistics on individual plant and national production of synthetic ammonia in Czechoslovakia prior to World War II. National production of synthetic aimnonia in 191+7 and 181+8 was reported by Czechoslovakia, and some logical estimates for 191+9 and 1950 have been made. These estimates are based largely on the requirements for the production of nitrogen fertilizer in Czechoslovakia as that production has .been reported. In this report, national estimates from 181+9 to 1951+ have been developed from individual plant estimates. The plant estimates for the period before World War II and for 191+6 througki 191+8 are considered firm, for they have been substantiated by reported and planned national production. Production since 191+9 has been esti- mated for each plant on the basis of plant intelligence showing increased activity, expansion, and rebuilding. The unusually broad range given for 1951+ production is dictated by the uncertainty sur- rounding the installation of major new facilities. For specific plant information, see Appendix A. b. Nitric Acid, Table 1+. All national production estimates have been derived from individual plant estimates. Plant estimates, in turn, are based on the comparatively well-known availability of synthetic ammonia, specific plant information concerning equipment and production of nitric acid, and the requirements for nitric acid. A large probable range of production is given because the estimates were indirectly derived. For specific plant information, see Appendix A. c. Fertilizer Nitrogen, Table 7. Estimates of production prior to World War II are taken from reliable. comprehensive statistics.. National production of nitrogen - 47 - S -E -C -R-E -T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 I Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 fertilizers was reported for 191+6 through 191+8, and logical estimates for later years .have been published. The Five Year Plan was also considered in making later estimates. Firm national production estimates were used to check indi- vidual plant estimates through 191+8. Since that time individual .plant estimates have been made on the basis of additional plant information indicating expansion, rebuilding, and production. Indi- vidual plant estimates now provide the basis for national production estimates. For spec~.fic plant information, see Appendix A. d. Ammonium Nitrate and Ammonium Sulfate Fertilizers from Synthetic Ammonia, Table Again, reliable pre-World War TI information helped by pro- viding a guide for this type of breakdown in production estimates. Up to 1939 the highest annual production of ammonium sulfate from synthetic ammonia amounted to the equivalent of 5,500 tons of nitro- gen. One plant is currently the only source of this particular fertilizer, and estimated production is believed to be between 4,000 and 7,000 tons of nitrogen. Gomparative],y firm production estimates for ammonium sulfate and calcium cyanamide account for a certain percentage of the total available fertilizer nitrogen. The remaining available nitrogen has been divided between. the major nitrate fertilizer, arrnnonium nitrate, and one category of "other nitrates." In all cases, these estimates were checked against available plant information. 2. Consumption Requirements. a. Synthetic Ammonia, Table 16. The estimate of the requirement for-the production of nitrogen fertilizers is comparatively firm. According to Table 7, 19,OOb tons of the fertilizer nitrogen produced during 1953 in Czechoslovakia will come from synthetic ammonia. This is equivalent to about 23,100 tons of ammonia, or 59 percent of the available supply. This figure includes that ammonia converted to nitric acid which, in turn, is converted to fertilizer. In this manner the nitro- gen contributed to fertilizer production by nitric acid (Table 17) is included in this estimate of 23,100 tons of synthetic ammonia. S-E-C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E-C-R-E-T The ~`emaining 41 percent of the available synthetic ammonia is then divided between explosives and miscellaneous industrial uses. This distribution estimate is considered logical but not. firm. The .allocation for explosives will cover the production of the required nitric acid (Table 17) plus the ammonia required for the production of perhaps 5,000 tons of ammonium nitrate at the Synthesis Plant. This much ammonium nitrate, in addition to the requirements for fertilizer,. is probably available there. b. Nitric Acid, Table 17. See the methodology used in the preparation of Table l~. Nitric acid provides the nitrate form of nitrogen for nitro- gen fertilizers. According to Table 8, production of ammonium nitrate fertilizer will require 11,000 tons of nitrogen during 1953? As 50 percent of this nitrogen is nitrate nitrogen, about 5,500 tons of nitrogen will be required from nitric acid. About 2,500 tons of nitrate nitrogen will also be required for the production of the "other nitrates." The total amount of 8,000 tons of nitrate nitrogen will be supplied by about 32,000 tons of nitric acid (100 percent. basis). Depending on the efficiency of the various processes involved, the probable range of this requirement for nitric acid is 31,000 to 34,000 tons. The remaining 1,500 tans Of the available nitric acid will provide the well developed explosives industry with about 11,000 tons, and 5,500 tons will be available for miscellaneous uses. These las-~ two estimates of requirements are considered logical in view of the sizes of the consuming industries, but they are not firm. -49- S-E -C -R-E -T Approved For Release 1999/09/02 :CIA-RDP79-01093A00040.0180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E-C-R-E-T APPENDIX D GAPS IN TNI'ELLIGENCE The productive capacity for fixed nitrogen at the older plants in Czechoslovakia is relatively well known. It would be of great value, however, to know the current rate of production of bath syn- thetic ammonia and nitric acid. For this purpose, information con- cerning actual production at the individual plants will be most helpful . The most glaring gap in intelligence on these strategic com- modities is the status of new plants. Confirmation of the relation- ship between the Stalin Works and the Nitrogen Products Plant at Lovosice is needed. If original plans are being followed, the new synthetic ammonia plant at the Stalin Works will eventually-double the previous national production .of synthetic ammonia. Thus it is essential that information concerning the capacity and production of this plant be obtained. It will also be important to obtain more information concerning production at the Nitrogen Products-Plant at Lovosice. What specific nitrogen fertilizers are produced? How much? It can be assumed that Within a very few years a new instal- lation for the production of nitric acid will. be erected, probably at Lovosice. It will be extremely important to know the capacity of such a plant, particularly for the possible production of con- centrated nitric acid, and to know the date the plant begins operation. S-E-C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E-C-R-E-T APPENDIX E SOURCES AND EVALUATION OF SOURCES 1. Evaluation of Sources. The United Nations Relief and Rehabilitation Administration report, Estimated Post-War Import Requirement"s of Czechoslovakia .for Chemicals and Allied Products, provided valuable, reliable, and comparatively detailed information concerning the fixed nitrogen industry of Czecho- slovakia prior to World War II. Many of the statistics contained in this report were originally published as official Czechoslovak statistics. Of the postwar intelligence reports, the most complete and reliable is a CIA SO document which has been translated by FDD. This CIA SO document contains miscellaneous official documents related to current and planned activities of the chemical industry in Czechoslovakia as of 1948. They were drawn up by a technical commission and are con- sidered reliable except that many of the plans have been altered or~ have not been achieved on schedule. Since 1949, information concerning this .industry has been available 25X1rgely as reports of activities at individual plants. The various stract services, including have provided the most regular informs ion o t Zs type. Since 1951, defector interrogations have provided an increasing number of valuable reports concerning individual plants. 2. Sources. Evaluations, following the classification entry and designated 'oval.," have-the following significance: S-E -C -R-E -T 25X1X7 FOIAb~ Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180~001-5 S-E-C-R-E-T A - Completely reliable B - Usually reliable C -Fairly reliable D - Not. usually reliable E - Not reliable F -Cannot be ,judged 6 - Cannot be fudged Doc. - Documentary 1 - Confirmed by other sources 2 - Probably true 3 - Possibly true 4 - Doubtful 5 - Probably false "Documentary" refers to original documents of foreign governments and organizations; copies or translations of such documents by a staff officer; or information extracted from such documents by a staff officer, all of which will carry the field evaluation "Docu- mentary" instead of a numerical grade. Evaluations not otherwise designated are those appearing on the cited document; those designated "RR" are by the author of this report. No "RR" evaluation is given when the author agrees with the evaluation on the cited document. 3? 4. State, Vienna Despatch No. 4~+2, 25X1A2g Aug 1952) . S. Eval. RR B-2. Sep 1952 (info.. Army, EUCOM, '7707 ECIC, RT-272-52, ICF-13626, 14 Apr 1952 (info., Jan 1952) (CIA C-10399). S: Eval. RR F-2. 25X1A2g 5. State, Vienna Despatch No. ~+~+2, op. cit. 25X1A2g S -E -C -R-E -T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E-C-R-E-T 6. FAO, Commodity Series, Fertilizers, Bulletin 17, Sep 1949. U. Eval. RR B-3. United Nations Relief and Rehabilitation Administration, Estimated Post-War Im ort Requirements of Czechoslovakia for Chemicals and Allied Products, 19 C. Eval. RR B-2. 7. Czechoslovak Republic, Statni Urad Statisticky, Statistical .Digest of the Czechoslovak Republic, Prague, 19 , p. . U. Eval. RR F-2. 8. United Nations Relief and Rehabilitation Administration, op. cit. 9. CIA. FDD, Special Translation, No. 15, 5 Apr 1951 (Czechoslovak Five-Year Plan for Agriculture, 1948), p. 67. S. Eval. RR F-2. 10. United Nations Relief and Rehabilitation Administration, off. cit. 11. Czechoslovak Republic, Statni Urad Statisticky, off. cit., pp. 51, 58, and 88. 12. Aikman, Ltd,, Fertilizer Reports, London, 1949-52. U. Eval. RR B-3. 25X1A2g 14. MSA, Vienna, TOMUS D-100, 19 Jan 1953 (CIA 1103759)? R. Eval. RR B-2. State, Paris Despatch No. 1136, 22 May 1950. S. Eval. RR B-2. ~~~aris Despatch No. 341, 6 Aug 1951. S. Eval. RR B-2. S a e, ienna Despatch No. 673, 18 Jan :1951. U. Eval. RR B-2. Chemische Industrie, Vol. 6, Berlin, Jun-1952, p. 426.. U. Eval. RR C-2. 15. United Nations Relief and Rehabilitation Administration, op. cit. 16. CIA FDD, Special Translation, No. 15, op. cit. 17. Czechoslovak Economic Bulletin, No. 26+x, Prague, 1 Feb 1953? U. Eval. RR C-l. lg. Ibid. 20. Tariff Commission, Chemical Nitrogen, Report No. 114, Second Series, 1937, p. U. Eval. RR A-2. -55- S-E-C-R-E-T 25X1A2g Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S -E -C -R-E -T 21. CIA/RR 24, The Nitric Acid Industry in the USSR, ~+ Jun 1953, p. 21. S~ US OFFICIALS ONLY. Eval. RR B-3: 22. A.M. Dubovitskiy and A.I. Shereshevskiy, Tekhnologiya mineral'nykh udobreniy (Technolo~,y of Mineral Fertilizers), Moscow-Leningrad, 19 , p. 316. U. Eval. RR F-2. 23. Ibid., p. 281. 24. Ibid., p. 263. 25. Ibid., p. 361. 26. NIE 90. S. Eval. RR B-3. 27. State, Paris Despatch No. 2185, 7 Feb 1951. C. Eval. RR F-2. Air, USAFE, OSI, IG, Wringer Report No. 49-15-642-0650, 16 Jun 1950 (info., May 1949). S. Eval. RR F-2. Arrr~y, USFA, ID-HQ, IBI-C166-L/8i4, Aug 1949. C. Eval. RR F-3. CIA IR Microfilm 1137, I.G. Farben Economic Studies (info., 1938). C. Eval. RR F-3. United Nations Relief and Rehabilitation Administration, 31. lb id. 32. United Nations Relief and Rehabilitation Administration, off. cit. 33. Memorandum from an executive of US chemical engineering Association of British Chemical Manufacturers, Report on Mission to Czechoslovakia, 1948. S. Eval. RR B-2. -56- S-E-C-R-E-T 25X1A2g 25X1A2g 25X1A2g Approved For Release 1999/09/02 :CIA-RDP79-01093A00.0400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E-C-R-E-T 25X1A2c Army, EUCOM, 7707 ECIC, RT-533-52, 17 Jun 1952 (CIA C-10770). S. Eval. RR F-3. 25X1A2c US Strategic Bombing Survey, Oil Division, Powler, Explosives, S ecial Rocket and Jet Pro ellants, War Gases and Smoke Acid, Jan 19 7. U. Eval. RR B-2. Army, USFA, G-2, R-994-53, 13 Mar 1953 (info., May 1952). S. Eval. RR F-3. 34. Association of British Chemical Manufacturers, op. cit. 35 ? Ibid. 36. Ibid. 37. Ibid. 38. Memorandum from an executive of US chemical engineering firm,. Nov 1948. S. E val. RR B-3. 25X1A2g E.R. Riegel, Industrial Chemistry, New York, 1949, p. 123. U. Eval. RR B-2. State, HICOG, Frankfurt Despatch No. 2519, 12 Mar 1951 (info., Oct 1950). S. Eval. RR F-2. Association of British Chemical Manufacturers, op. cit. 25X1A2g Army, USFA, Special Bi-weekly Report, No. 124, 18 Aug 1950. S. Eval. RR F-3. 39. State, HICOG, Frankfurt Despatch No. 2.519, op. cit. 40. 25X1A2g 41. 42. 43. 44. S-E -C-R-E-T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 S-E-C-R-E-T 45. State, Paris Despatch No?. 2185, op. cit. 46. 47. .The New York Times, 8 Dec 1952. U. Eval. RR B-2. Rude Pravo, No. 310, Prague, 20 Nov 1952. U. Eval. RR F-3. ArtrXy, MA, Prague ~ R-1-51, 9 Jan 1951 ( info . , Dec 1950 . 48. The New York Times 49. 51. Ibid. 52. Chemical Construction Co., A Brief Survey of the World's Synthetic Ammonia Capacities, 19 9-1950, New York, p. C. Eval. RR B-1. 25X1A2g 25X1A2g 25X1A2g - 58 - S -E -C -R-E -T Approved For Release 1999/09/02 :CIA-RDP79-01093A000400180001-5 Approved For Release 1999/09/02 : CIA-RDP79-01093'A000400180001-5