Ruthenium Melt Catalysis PRODUCING CHEMICALS FROM SYNTHESIS GAS By John F. Knifton Texaco Chemical Company, Austin, Texas
A range of commodity chemicals and fuels can be generated directly from synthesis gas by ruthenium melt catalysis. Careful selection of the catalyst components enables a wide range of oxygenates to be produced, while other advantages of this flexible process include high productivity and the ease with which the products may be recovered and the catalyst recycled.
In platinum-metal catalysed organic syn- present a renewable surface may avoid many of thesis, the primary purpose is to produce pure the problems of deactivation seen with con- products in high yields, with good ventional heterogeneous catalysts (4). reproducibility and ease of product isolation. Frequently, the melt is called upon to play While both homogeneous and heterogeneous more than one role in a chemical process. It catalysis systems may fulfill these roles in may, for example, simply act as a solvent for laboratory or industrial processes, an alterna- reactants and products; it may be a catalyst; it tive approach, that has many of the inherent may supply one or more of the reactants, as well advantages of both systems, is the use of molten as aid in controlling the heat of reaction. The salts as catalyst and/or reaction media. salts may be used singly (for example molten Molten salts may be classified into simple Na2C03, ZnCL or AlC13), or as eutectic ionic salts (for example the alkali and alkaline mixtures (such as Li2C03-Na2C03-K2C03, earth metal halides), simple and polymeric CuC1-CuCl2-KC1, and AlC13-BuPyC1) where oxyanionic salts (such as metal nitrates, car- the lower liquidus temperatures may be bonates, phosphates, borates), and salts contain- advantageous. ing organic cations and/or anions (including the Molten salts have already found numerous quaternary phosphonium and ammonium salts) technical applications in industrial catalytic (I). The high thermal stability of many of these processes. Examples include the Transcat, melts, together with their low vapour pressure, Deacon and SO2 oxidation processes (I ,2). The good thermal and electrical conductivity, and literature illustrating the diverse uses of melt low viscosity provides them with a range of catalysis with the platinum group metals important physical and chemical advantages includes applications in chlorination (z), oxida- over conventional homogeneous and tion (5) and selective hydrogenation (6) process- heterogeneous catalyst systems (2). Molten ing, as in Equation i: salts, such as the quaternary phosphonium n salts, dissolve a broad range of metals, oxides and complexes; high reaction rates and yields are often possible (for example organic syn- U theses in molten tetrachloroaluminate solvents In the case of synthesis gas (carbon (3) and fused alkali metal salts (4)) with ease of monoxide/hydrogen) chemistry, Fischer- producdcatalyst separation and recovery. Tropsch production using Ir4(C0)12dissolved Where chemical synthesis occurs at a melt-gas in NaC1-AlC13 melts has now been demons- interface, as in gas reactions, the ability to trated (7); ethane is the major product fraction,
Platinum Metals Rev., 1985,29, (2), 63-72 63 see Equation ii or, under flow conditions, ease of product-catalyst separation, typical of isobutane and propane. A further examination, heterogeneous catalyst systems, once the reac- by Collman and his colleagues, implicates tion is complete. chloromethane (or methanol) as the primary Optionally, a second or third transition metal intermediate, with methane, ethane, and may be added to the ruthenium to further chloromethane the major carbon-containing modify its performance and to steer the product products (8). distribution toward specific aliphatic CO + 3H2 ->C~HL (major) + CH4 + oxygenates. These modifiers may be derivatives C3Hs (tr) + C4Hlo (tr) ii of rhodium, cobalt, manganese, rhenium, Ruthenium Melt Catalysis zirconium and titanium, in either halogen-free In other, potentially far-reaching applica- or halogen-containing forms. tions of melt catalysis by the platinum group Some specific applications of this technology metals, we at Texaco have demonstrated the include (Equations iii to viii): synthesis of a range of commodity chemicals [I] Ethylene glycol synthesis directly from and fuels directly from synthesis gas by the use synthesis gas using ruthenium-rhodium catalysts of ruthenium-containing molten salt catalysis. or ruthenium alone (9). Products include ethylene glycol, C1-C4 [2] C1-G AlcohoVacetate ester fuel alcohols, acetic acid, acetate esters, C2+ olefins products, which are potential octane enhancers, and vicinal glycol esters. In its simplest form, using ruthenium in combination with cobalt, this new class of melt catalyst comprises one or titanium or zirconium (I 0). more ruthenium sources, including ruthenium [3] Selective methanol production with the carbonyls, oxides and complexes dispersed in a lowmelting (m.p. solid under ambient conditions. mole) m ( [B] The quarternary salt melts below the m temperatures of carbon monoxide hydrogena- tion so that, under typical operating conditions, ln it is a highly polar, non-volatile, liquid media PRODUCTIVITY
that readily solubilises the ruthenium catalyst A precursor and the synthesis gas components, thereby ensuring rapid rates of carbon ETHERS, monoxide hydrogenation to the desired ali- phatic oxygenates. *GLYCOL [C] Optionally, upon cooling, the N rutheniumquarternary salt may resolidify, GLYCOL allowing ease of separation of the liquid organic - products from the solid inorganic catalyst com- ponents by decantation or distillation. ETHYLENE 05 1.0 15 20 The melt catalyst enjoys, thereby, certain of RHODIUM OR RUTHENIUM CONTENT (m mole) Fig. 1 Ethylene glycol synthesis from the intrinsic advantages of both homogeneous synthesis gas showing the effect on and heterogeneous systems; the inherent high productivity of the ruthenium-rhodium selectivity and reproducibility of liquid catalyst molar ratio homogeneous catalysts under normal carbon Effect of varying rhodium, 0; Effect of varyine ruthenium x monoxide hydrogenation conditions, and the
Platinum Metals Rev., 1985,29, (2) 64 ruthenium-manganese combination (10, I I). advantages of the mixed ruthenium-rhodium [4] Acetic acid production directly from syn- system include improved glycol productivity thesis gas catalysed by halogen-promoted and ability to operate at lower synthesis gas pre- ruthenium-cobalt combinations (I I). ssures. It may be noted that (see Table I): ... (I) CH20H 111 The productivity of the ruthenium- I rhodium melt catalyst is high; liquid weight CH2OH gains may exceed 200 weight per cent (expt. 2) Ru + Rh and turnover frequencies surpass 5 x 10-7s at C.H2.+ ]OH + CnH2"+]OAc iv / 220°c. corn2 (2) Glycol : alkanol weight ratios of I : I .37 have been realised (expt. 6). (3) Both alkanol and diol products may be V readily isolated by fractional distillation of the crude liquid product and the solid residual Ru + Co + I vi yc;3cooHruthenium-rhodium catalyst recycled. Through the addition of aliphatic carboxylic The primary requirements in selecting the acid coreactants, this chemistry may be further quaternary Group VB salts (Table I) as suitable extended to: reaction media are that they be thermally stable [5] The production of vicinal glycol esters under typical carbon monoxide hydrogenation (Equation vii) (I 2). conditions and that they melt below the reaction [6] The generation of ethylene and propylene temperature (200 to 25oOC) to give stable, from synthesis gas (13) by a novel two-step highly polar, fluid media for- solubilisation of procedure involving the intermediate genera- the transition-metal component. tion of ethyl and propyl esters (Equation viii). Figure I illustrates how both the ruthenium CH200CR vii and rhodium catalyst components are beneficial to the formation of ethylene glycol, expressed here in terms of total glycol +glycol ether CO/H2 + RCOOH P200CR productivity, for the Ru(acac) ,-Rh(acac) d BuJBr catalyst precursor. Maximum glycol kCIEOOCR+ production is achieved with increasing rhodium A +C 2H 4 Vlll... addition, up to rhodium: ruthenium ratios of -+ C3H700CR C3H.5 about I:I. Very little diol is generated, however, in the absence of either the ruthenium Ethylene Glycol component (see Figure I), or the quaternary Ethylene glycol commands a 4.5 x 109 Ib/yr phosphonium salt (Table I, expt. 5). While the market in the United States of America, and presence of ruthenium is necessary to the while this largevolume petrochemical is pre- formation of glycol, the data of Figure I, sently generated entirely by ethylene oxide together with the isolation of mixed ruthenium- hydrolysis, there has been considerable research rhodium clusters such as RU~R~(CO)]~(9), activity during the past decade into alternate point to the role of the second metal, rhodium, routes to polyhydric alcohols either directly, or in providing improved diol selectivity. indirectly, from synthesis gas. We have demons- trated the preparation of ethylene glycol and its Alcohol-Ester Fuels monoalkyl ether derivatives from synthesis gas A second class of platinum metal melt (Equation iii) using ruthenium or a ruthenium- catalysts-comprising a ruthenium source, rhodium catalyst combination dispersed in a such as Ru~(CO)U,optionally in combination low-melting quaternary phosphonium salt such with a halogen-free cobalt, titanium, zirconium, as tetrabutylphosphonium bromide. The manganese or rhenium component, dispersed
Platinum Metals Rev., 1985,29, (2) 65 Platinum I Table I Ethylene Glycol from Synthesis Gas via Ruthenium-Rhodium“Melt” Catalysisa Merais
Productyield, mrnole
Rev., c A Melting CH,OH CH,OH - Total liquid 2 point,” I I yield, Expt. Ruthenium-rhodiumsource Quaternarysalt OC CH,OH CH,OR~ MeOH EtOH weight per centd
~ N 1 Ru(acac),-Rh(acac), Bu,PBr 100 77.2 62.6 2 50 168 189 ,--.W vN 2 Bu,PI 96 80.4 41.6 312 237 214
3 C,,H,,Bu,PBr 54 11.4 42.8 295 228 176
179 0.5 0.4 0.1 0.7 -=3 141 “ I C,H,,Ph,PBr I None 0.2 - 8.9 0.9 e
6 Bu,PBr 1oof 30.3 14.3 96 23 57
Charge: ruthenium 4.0 mmole: rhodium 2.0 mmole: R,PX 159: run conditions: 220°C: 430 atm constant pressure; Corn, (1 : 11: 618 hr. Melting point of quatemav salt must be substantially below the reaction temperature (220°CI. - - Ethylene glycol monoalkyl ether. HOCH,CH,OR:R = Me. Et. Liquid yield Iwt %Icalculated basis total weight of catalyst + quaternary salt charged. Product liquid is > 90% water. Run time. 2 hr. in a quaternary phosphonium salt-has been as well as environmental problems (I0). In our found to be effective for the selective synthesis work, we have focused on two c1-c3 of (a) methanol, (b) ethanol and (c) their acetate alcohoVester blends produced by carbon esters directly from synthesis gas (see Table 11). monoxide hydrogenation (Equation iv) using the These liquid products are intended for use as Texaco melt technology. The first blend (see octane enhancers for gasoline. The shift to Table 111, product mix “A), rich in methanol unleaded and low-leaded gasoline in both the and ethanol, is similar in composition to those United States and Europe will likely raise the prepared by the procedure of Table 11, expt. 7. clear octane requirements by about two octane The second blend (“B”) contains sizeable numbers. Although some of this increase could quantities of methyl and ethyl acetates, and be satisfied by higher severity processing, more closely resembles the products of Table 11, octane improvers, particularly liquid aliphatic expt. 9, generated using a rutheniumcobalt oxygenates, are becoming an increasingly couple. Both blends are, of course, the products attractive alternative. of numerous runs under standard operating Here it may be seen from an inspection of the conditions; they have been isolated with the summary data in Table I1 that: minimum of fractionation. (I) Ethanol may constitute near 60 per cent Preliminary performance data for the two of the crude liquid product with 76 per cent blends indicates: being CI-CJ alcohol, when employing the (a) The octane improvement properties of Ru02-Bu4PI couple (expt. 7). The the C1-C3 alcohol mix, “A”, appear to be good, rutheniudhalide-free titanium/Bu4PBr com- and on this basis it may show promise as a bination likewise produces C1-C3 alcohols in future octane blending agent. The improve- 61 per cent selectivity of which up to 66 per ments in motor octane number (AMON) and cent is ethanol (expts. 10and I I). research octane number (ARON) values, about (2) A balanced mix of CI-C3 alcohol and 1.4 and 3.4, respectively, for mix “A”, are acetate esters may be realised in high yields noticeably higher than those for composite using a variety of ruthenium-cobalt bimetallic alcohol-ester mix, “B”, but the increase in catalysts as illustrated here by expts. 8 and 9. volatility is greater for the alcohoVester gas- (3) Methanol will be the predominant oline blend (14). product fraction when the melt comprises (b) The oxidative stability and gum-forming ruthenium plus a halogen-free manganese or tendencies of the gasoline-containing rhenium component. With RuO rRe4CO) ~d alcohoyester mix appear poorer than for gas- Bu4PBr (expt. 12), methanol selectivity in the oline containing mix “A”. Stability of mix “A” liquid product is 85 per cent and the turn- is equivalent to that of gasoline (14). over frequency is 24 mol MeOWg atom (c) The alcohol composition in gasoline rutheniudhr. exhibits superior corrosion properties, when (4) The addition of certain solvents may lead compared to “B” blend, for each of the metals to further changes in product composition. The commonly used in automotive engine surfaces. presence of added pdioxane, for example (expt. I 4), makes ethyl acetate the predominant Acetic Acid product, with alkyl acetates providing 67 per Acetic acid is another commodity chemical cent of the organic liquid fraction. with a large market requirement, of about Numerous factors must, of course, be con- 2.9 x 109 lb/yr in the US., that has been sidered in the selection of organic oxygenates as targeted as being potentially made directly from blending components in gasoline, particularly synthesis gas (Equation vi) (IS), rather than by cost, octane blending value, volatility, water methanol carbonylation or through oxidation and gasoline compatibility, raw material chemistry. We have established that acetic acid availability, engine performance and corrosion, may be generated directly from synthesis gas as
Platinum Metals Rev., 1985,29, (2) 67 Platinum Table II Alkanols Plus Acetate Esters from Synthesis Gasa Metals
Liquid product composition,weight per centC Rev., Melting Alcohols Acetate esters Liquid point yield, 1985,29, Expt. Catalyst precursor Quaternarysalt OC MeOH EtOH EtOAc PrOAcb per cent
7 RuO, Bu,PI 96 12.9 59.5 6.4 0.6 151 (2) 8 RuO,-Co(acac),d Bu4PBr 100 10.2 28.2 19.9 9.5 215
9 Ru,(CO),,-CO,(CO)~~ Bu4PBr 100 9.3 29.1 21.1 11.9 230
10 RuO,-Ti(acac),(OBu), Bu,PBr 100 16.3 40.7 8.0 4.3 169
11 RuO,-Ti(OMe), Bu,PBr 100 21.0 39.0 5.4 3.6 6.1 3.1 239
12 RUO,-~R~,(CO)~~ Bu,PBr 100 84.7 9.4 0.4 0.3 85 I 13 RuOZ-8MnCO, Bu,PBr 100 86.3 2.3 I 1.3 0.5 85
14 RuO,-$O,(CO),~ C,H,,Ph,PBr 179 4 4.0 7.0 54.0 6.0 <1 1
:Typical operatingwnditions: 220'C: 430 atm constantpressure; CON, I1 : 1I: catalyst charge: ruthenium 2-8 mmole. quaternarysalt. 1(t25 g Small quantitiesof methyl propionateand ethyl propionatepresent in these fractions. Liquidyield (wt %1calculated basis total catalystcharge. Operatingpressure. 272 atm. Run in p-dioxanesolvent. operating pressure544 am. Table 111 AleohoVEster Fuels from Synthesis Gas
Volume per cent
Product mix "A' Product mix "B' Component C,-C, alcohols C,-C, alcohol/esters
Methanol 46.6 30.3
Ethanol 40.4 22.1
iso-Propanol - 1 .o
n-Propanol 1.4 2.2
n-Butanol - 3.5
n-Pentanol - 1.9
Methyl acetate 0.7 13.4
Ethyl acetate 2.3 15.5b
Propyl acetate - 10.lb
Higher oxygenates 8.68 -
100.0 100.0
Includes: 1.I-dioxolans and its alkyl derivaliws. elkoorymathanas. alkoxvethanss.alkyl formatea and alkyl proplmat0s Includes 601110 alkyl propionatas.substituted dioxolanes. mono and dialkoayerhanes. and dialkoaymerhanea. the predominant oxygenate product in 68 manufacture by the regioselective carbonyla- weight per cent selectivity (~t) using tion of n-olefins (Eq. ix). Preferred catalyst Ru >(CO)1rCoz(C0)$Bu 4PBr melt catalyst, formulations include bis(tripheny1phosphine) preferentially where the cobalt :ruthenium and palladium(I1) chloride and its para-tolyl carbon monoxide :hydrogen ratios exceed unity analogue, PdC1d(pCH3.&H4),],, dispersed in (for example see Figure 2). tetraethylammonium trichlorostannate(I1). In the case of nonanoate ester synthesis, yields Short-Chain Fatty Acids consistently exceed 80 mole per cent for both Platinum group metals dispersed as melt systems (16)~and carboxylic acid linearity is catalysts have also been utilised by Texaco in a greater than 80 per cent. A variety of alkene novel process for making short-chain (C5-CIo) and alkyne structures may be carbonylated in fatty acids (SFAs). Now generated from coconut the presence of different alkanol coreactants oil and through 0x0 chemistry, these SFAs find (see Table IV). expanding applications in the synthetic RCH = CHz + CO + R'OH 4 lubricant and plasticiser markets. R-CHrCH KOOR' ix We have demonstrated that ligand-stabilised The palladium catalyst, P~C~~[P(C~HJ)&- palladium and platinum salts dispersed in I O[(C~H~)~~~S~C~J,exists under carbonyla- quaternary Group VB salts of trichlorostan- tion conditions (Table IV) as a clear, nate(I1) are effective catalysts for SFA homogeneous, phase with the n-olefin and
Platinum Metals Rev., 1985,29, (2) 69 Platinum Tablo IV Alkene/Alkyne Carbonylation Catalysed by PdCI,[ P(C,H,),],-IO[ (C,H,),N] [ SnCI,Ia Metals
:onversion
Rev., mole Selectivity Yield. Expt. Alkene/alkyne Alkanol per cent Identity per centb mole per cent 1985,29, 17 1-Hexene Ethanol 51 Ethyl heptanoate 79.2 51
18 1-0ctene Ethanol 84 Ethyl nonanoate 86.3 62 (2) 19 1-Tetradecene Ethanol 86 Ethyl pentadecanoate 90.9 64
20 3,3-Dimethyl-1 -butene Ethanol 40 Ethyl 4.4-dimethylpentanoate 99.5 36
21 2.4.4-Trimethyl-1 -pentene Ethanol 28 Ethyl 3.5.5-trimethylhexanoate 96.1 23
22 4-Methylcyclohexene Ethanol 80 Ethyl 4-methylcyclohexane carboxylated 80.0 42
Ethyl 2-methylheptanoate 57.2 23 cis-2-HepteneC Ethanol 72 41 Ethyl octanoate 24.2
Ethyl 1-heptene-2-carboxylate 62.3 24 1-Heptynec Ethanol 96 Ethyl 2-octenoate 37.7 39
25 1-0ctene 2-Chloroethanol 51 2-Chloroethyl nonanoate 80.7 21
26 1-0ctene 2-Propanol 58 lsopropyl nonanoate 91.1 46
27 1-0ctene n-Hexanol 85 n-Hexyl nonanoate 85.8 57
28 1-0ctene Phenol 72 Phenyl nonanoate 83.2 14
Run conditions: [alkane]:[ethanol]: [palladium] = 100:2001; 100elm: 85% 8 hr. Seiectivity calculated basis total acid ester pmduct. Initial lalkene or alkynel : [palladium] = 50 : 1: 1-heptyne reaction time 4 hr. 40 Minor product: ethyl 3-methylcyciohexane carboxylate. Fig 2. The generation of 50 acetic acid from synthesis gas illustrating the effect of the cobalt: ruthenium catalyst molar ratio Product Profile: acetic acid, x methanol, A ethanol, o propanol, v methyl acetate, o ethyl acetate, o
0.5 1.0 1.5 2.0 COBALT : RUTHENIUM alkanol coreactant. However, this particular does allow multicycling of the palladium melt quaternary salt melts at 78OC, so, following car- catalyst, over 30 to 40 cycles, with little overall bonylation, the reactant mixture may be cooled loss in specific activity. to reprecipitate the inorganic catalyst com- The economic attractiveness of the Texaco ponents, thereby once again ensuring ease of SFA process(Equati0nix) has been reviewed( I 8). separation of the crude product acid esters from the now resolidified palladium catalyst. Conclusions Intrinsic advantages of this case of car- Clearly the myriad potential applications of bonylation catalyst over its solvent-solubilised the platinum group metals in melt catalysis has counterparts (I 7) would be in: only just begun to be explored. The develop- (I) The ease of product acid ester separation. ment of new classes of catalysts to produce ali- (2) Improved stability of the palladium phatic oxygenates from synthesis gas, beyond catalyst during multicycling. the generation of C& alkanolddioldacids to (3) Potentially higher concentrations of more complex molecules, and their use with N-, active palladium within the reaction mix. P- and S-containing coreactants, are challenges The long-term life of these palladium- for the future. The extension of this technology dispersed molten salt catalysts, particularly to oxidation, halogenation and refinery PdClz[P(C6H 5)3]2-((C~Hr)&JISnCl 31, has in fact processes, particularly hydrocracking and been confirmed in multicycling experiments, isomerisation, has yet to be fully exploited. with regeneration of spent palladium catalyst The commercialisation of the novel syngas- (particularly reoxidation of inactive Pd(0) to-aliphatic oxygenate processes outlined in this species) by treatments with mineral acids, article will hinge primarily upon future peroxides, chlorination and oxychlorination economic projections, particularly the relative techniques. Chlorination in the presence of feedstock values of petroleum, versus coal- or added chlorinated solvent (I 6), in particular, natural gasderived synthesis gas.
Platinum Metals Rev., 1985,29, (2) 71 References
I B. W. Hatt and D. H. Kerridge, Chem. Br., 1979, 10 J. F. Knifton, R. A. Grigsby, and S. Herbstman, 159(4378 Hydrocarbon Process., 1984~63,(I), I I I 2 C.N.Kenney, Catal.R~.Sci.Eng.,197~,11,1g7 I I J. F. Knifton, R. A. Grigsby, and J. J. Lin, 3 H. L. Jones and R. A. Osteryoung, “Advances in Organometallics, 1984,3, (I),62 Molten Salt Chemistry,” Vol. 3, ed. J. Braunstein, 12 J. F. Knifton, J. Catal., 1982, 76, (I), 101; G. Mamantov, and G. P. Smith, Plenum Press, 3. Chem. SOC.,Chem. Commun., 1981,(4), 188 New York, 1975,Chapter 3 13 J. F. Knifton,?. Caral., 1983,79,(1),147 4 J. E. Gordon, “Techniques and Methods of 14 J. F. Knifton, R. A. Grigsby, and S. Herbstman, Organic and Organometallic Chemistry,” Vol. I, in “Catalytic Conversions of Synthesis Gas and ed. D. B. Denney, Marcel Dekker, New York, Alcohols to Chemicals,” ed. R. H. Herman, 1969,Chapter 3 Plenum Press, New York, 1984, p. 81 5 P.R.Rony, Ann. N.Y.Acad.Sci.,1970,17~,238 15 J. Haggin, Chem. Eng. News, 1981,59, (23), 23; 6 G.W.Panhall,3.Am.Chem.Soc.,1972,94,8716 198 1 > 59, (46), 57 7 G. C. Demitras and E. L. Muetterties, J. Am. 16 J. F. Knifton, J. Am. Oil Chem. SOC.,1978, 55, Chem. Soc., 1977~99,(81,2796 (s), 496 8 J. P. Collman, J. I. Brauman, G. Tustin, and 17 J. F. Knifton,J. Org. Chem., 1976,41, (s), 793; G. S. Wann, J. Am. Chem. SOC., 1983, 105, J. Org. Chem., 1976,41,(17), 2885 3913 18 “Fatty Acids and Derivatives,” Chem Systems 9 J. F. Knifton, J. Am. Chem. SOC.,1981, 103, (13), Report#78-2 (January 1979); A. G. Johanson, 3959;J.Chem. SOC.,Chem. Commun., 1983,729 J. Am. Oil Chem. SOC.,1977,54, (II), 848A Platinum Compounds in Cancer Chemotherapy A seminar on “Organometallic Compounds spectrum of tumour activity compared to the in Cancer Chemotherapy” took place at the parent drug. However, Dr. Cleare felt that Physikzentrum, Bad Honnef, West Germany, improved activity should be the subject of on March 4th and 5th 1985.It was sponsored research aimed at a third generation platinum by the Heraeus Foundation set up for the drug. A likely approach was to design targeted furtherance of scientific research by Wilhelm platinum complexes with some biological Heinrich Heraeus, grandson of the founder of selectivity towards tumour cells. In this regard, the German precious metal and speciality Professor J. Karl of Regensburg University chemical company W. C. Heraeus G.m.b.H. described some elegant studies aimed at Inevitably platinum complexes dominated the developing platinum complexes with specific proceedings. activity towards hormone dependent breast The clinical importance to date of cisplatin cancers. Platinum complexes have been syn- was summarised by Professor S. Seeber thesised using ligands which have proven (University of Essen). After reiterating the sig- ability to bind covalently to estrogen receptor nificance of the drug in the treatment of genito- sites. This work could be of significance in urinary tumours, he went on to indicate its extending platinum drug activity but caution potential use in combination with other drugs must be expressed; a genuine advantage of com- in the treatment of certain types of lung cancer, plex over free ligand has yet to be established. including small cell, adeno- and epidermoid Active platinum complexes with bidentate carcinomas. Promising results are also being organic diamine ligands were described by Dr. obtained on rarer oesophageal tumours. H. Brunner of Regensburg University and Dr. Dr. M. J. Cleare (Johnson Matthey) sum- H. A. Meinema (TNO-Utrecht). marised the current status of analogue studies. The reaction of platinum compounds with Second generation drugs have clearly emerged DNA seems to hold the key to their anti-cancer on the basis of comparable therapeutic activity activity. Dr. N. P. Johnson of CNRS, Toulouse to cisplatin associated with considerably and Dr. B. Lippert of the Technical University reduced toxicity. Of these carboplatin (JM8) at Munich, discussed studies on model Pt-DNA was the most advanced. Data from numerous adducts. It appears clear that the primary clinical trials suggest that JM8 will be site of DNA attack is the N7 position on registered for use in ovarian cancer in the near guanine. Ninety per cent of the mono- future. There is evidence to suggest that some functional platinum lesions rapidly chelate with of the cisplatin analogues, particularly another adjacent purine base (primarily but iproplatin (JM9), may have a slightly different not exclusively guanine). M.J.C.
Platinum Metals Rev., 1985,29, (2) 72