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    • 2. 发明授权
    • Process for selective formation of C.sub.4 compounds and biphosphine
disulfide-containing catalyst system used therein
    • 用于选择性形成其中使用的C4化合物和含二硫化碳的催化剂体系的方法
    • US4339609A
    • 1982-07-13
    • US215554
    • 1980-12-11
    • Wayne R. PretzerThaddeus P. KobylinskiJohn E. Bozik
    • Wayne R. PretzerThaddeus P. KobylinskiJohn E. Bozik
    • B01J31/24C07C29/32C07C45/49C07C27/22C07C45/50
    • B01J31/0231B01J31/1845B01J31/226B01J31/26C07C29/32C07C45/49B01J2231/641B01J2531/845B01J31/20B01J31/2208Y02P20/52
    • C.sub.4 compounds including n-butanol and n-butanal are produced by reacting methanol, hydrogen, and carbon monoxide, in the presence of a cobalt catalyst selected from the group consisting of (a) a cobalt carbonyl, (b) a hydrido cobalt carbonyl and (c) a cobalt-containing material convertible to a cobalt carbonyl or a hydrido cobalt carbonyl, an iodine promotor and a biphosphine disulfide having the formula: ##STR1## wherein R.sub.1, R.sub.2, R.sub.3 and R.sub.4, the same or different, are selected from the group consisting of saturated or unsaturated, staight or branched chain alkyl radicals having from one to 24 carbon atoms, cycloalkyl radicals having from three to 40 carbon atoms, aryl radicals having from six to 20 carbon atoms, aralkyl and alkaryl radicals having from six to 40 carbon atoms and halogen substituted derivatives thereof. A high degree of selectivity towards the formation of butanol and butanal is provided by using the cobalt entity and the biphosphine disulfide in a molar ratio in the range of about 2:1 to about 10:1, based on elemental cobalt and phosphorus. The reaction is conducted at elevated temperature and pressure conditions for a time sufficient to convert methanol to n-butanol and n-butanal.
    • 包括正丁醇和正丁醛的C 4化合物通过甲醇,氢气和一氧化碳在钴催化剂存在下制备,所述钴催化剂选自(a)羰基钴,(b)羰基钴和 (c)可转化为羰基钴或羰基钴的钴的物质,碘促进剂和具有下式的二膦化合物:其中R1,R2,R3和R4相同或不同,选自 由具有1至24个碳原子的饱和或不饱和,直链或支链烷基,具有3至40个碳原子的环烷基,具有6至20个碳原子的芳基,具有6至6个碳原子的芳烷基和烷芳基 40个碳原子及其卤素取代的衍生物。 以元素钴和磷为基础,通过使用摩尔比在约2:1至约10:1范围内的钴实体和二膦二膦来提供对形成丁醇和丁醛的高度选择性。 反应在升高的温度和压力条件下进行足以将甲醇转化为正丁醇和正丁醛的时间。
    • 5. 发明授权
    • Process for selective formation of C.sub.4 compounds and
thiol-containing catalyst system used therein
    • 用于选择性形成C4化合物和其中使用的含硫醇催化剂体系的方法
    • US4339610A
    • 1982-07-13
    • US215555
    • 1980-12-11
    • Wayne R. PretzerThaddeus P. KobylinskiJohn E. Bozik
    • Wayne R. PretzerThaddeus P. KobylinskiJohn E. Bozik
    • C07C29/32C07C45/49C07C27/22C07C45/50
    • C07C29/32C07C45/49C12C11/02Y02P20/52
    • C.sub.4 compounds including n-butanol and n-butanal are produced by reacting methanol, hydrogen, and carbon monoxide, in the presence of a cobalt catalyst selected from the group consisting of (a) a cobalt carbonyl, (b) a hydrido cobalt carbonyl and (c) a cobalt-containing material convertible to a cobalt carbonyl or a hydrido cobalt carbonyl, an iodine promotor and a thiol defined by the formula:RSHwherein R is selected from the group consisting of saturated or unsaturated, straight or branched chain alkyl radicals having from one to 24 carbon atoms, cycloalkyl radicals having from three to 40 carbon atoms, aryl radicals having from six to 20 carbon atoms, aralkyl and alkaryl radicals having from six to 40 carbon atoms and halogen substituted derivatives thereof. A high degree of selectivity towards the formation of butanol and butanal is provided by using the cobalt entity and the thiol in a molar ratio in the range of about 2:1 to about 10:1, based on elemental cobalt and sulfur. The reaction is conducted at elevated temperature and pressure conditions for a time sufficient to convert methanol to n-butanol and n-butanal.
    • 包括正丁醇和正丁醛的C 4化合物通过甲醇,氢气和一氧化碳在钴催化剂存在下制备,所述钴催化剂选自(a)羰基钴,(b)羰基钴和 (c)可转化为羰基钴或羰基钴的钴的物质,碘促进剂和由下式定义的硫醇:其中R选自饱和或不饱和的直链或支链烷基 具有1至24个碳原子,具有3至40个碳原子的环烷基,具有6至20个碳原子的芳基,具有6至40个碳原子的芳烷基和烷芳基及其卤素取代的衍生物。 基于元素钴和硫,通过使用钴实体和硫醇以约2:1至约10:1的摩尔比来提供对形成丁醇和丁醛的高度选择性。 反应在升高的温度和压力条件下进行足以将甲醇转化为正丁醇和正丁醛的时间。
    • 8. 发明授权
    • Process for selective formation of C.sub.4 compounds and organic
sulfide-containing catalyst system used therein
    • 用于选择性形成C4化合物和其中使用的含有机硫化物的催化剂体系的方法
    • US4339611A
    • 1982-07-13
    • US215556
    • 1980-12-11
    • Wayne R. PretzerThaddeus P. KobylinskiJohn E. Bozik
    • Wayne R. PretzerThaddeus P. KobylinskiJohn E. Bozik
    • B01J27/043B01J31/20C07C29/32C07C45/49C07C27/22C07C45/50
    • B01J31/2234B01J27/043B01J31/0218B01J31/0231B01J31/20B01J31/26C07C29/32C07C45/49B01J2231/34B01J2231/641B01J2531/845Y02P20/52
    • C.sub.4 compounds including n-butanol and n-butanal are produced by reacting methanol, hydrogen, and carbon monoxide, in the presence of a cobalt catalyst selected from the group consisting of (a) a cobalt carbonyl, (b) a hydrido cobalt carbonyl and (c) a cobalt-containing material convertible to a cobalt carbonyl or a hydrido cobalt carbonyl, an iodine promotor and an organic sulfide having the formula:R.sub.1 --S--R.sub.2wherein R.sub.1 and R.sub.2 can be the same or different members selected from the group consisting of saturated or unsaturated, straight or branched chain alkyl radicals having from one to 24 carbon atoms, cycloalkyl radicals having from three to 40 carbon atoms, aryl radicals having from six to 20 carbon atoms, aralkyl and alkaryl radicals having from six to 40 carbon atoms and halogen substituted derivatives thereof. A high degree of selectivity towards the formation of butanol and butanal is provided by using the cobalt entity and the organic sulfide in a molar ratio in the range of about 2:1 to about 1:10, based on elemental cobalt and sulfur. The reaction is conducted at elevated temperature and pressure conditions for a time sufficient to convert methanol to n-butanol and n-butanal.
    • 包括正丁醇和正丁醛的C 4化合物通过甲醇,氢气和一氧化碳在钴催化剂存在下制备,所述钴催化剂选自(a)羰基钴,(b)羰基钴和 (c)可转化为羰基钴或羰基钴的钴的物质,碘促进剂和有机硫化物,其具有下式:R1-S-R2,其中R1和R2可以是相同或不同的选自基团 由具有1至24个碳原子的饱和或不饱和的直链或支链烷基,具有3至40个碳原子的环烷基,具有6至20个碳原子的芳基,具有6至40个碳原子的芳烷基和烷芳基 原子和卤素取代的衍生物。 通过使用基于元素钴和硫的摩尔比在约2:1至约1:10范围内的钴实体和有机硫化物来提供对形成丁醇和丁醛的高度选择性。 反应在升高的温度和压力条件下进行足以将甲醇转化为正丁醇和正丁醛的时间。
    • 10. 发明授权
    • Process for selective formation of C4 compounds and thiol-containing
catalyst system used therein
    • 用于选择性形成C4化合物和其中使用的含硫醇催化剂体系的方法
    • US4447557A
    • 1984-05-08
    • US353376
    • 1982-03-01
    • Wayne R. PretzerThaddeus P. KobylinskiJohn E. Bozik
    • Wayne R. PretzerThaddeus P. KobylinskiJohn E. Bozik
    • C07C29/32C07C45/49B01J31/20
    • C07C29/32C07C45/49Y02P20/52
    • C.sub.4 compounds including n-butanol and n-butanal are produced by reacting methanol, hydrogen, and carbon monoxide, in the presence of a cobalt catalyst selected from the group consisting of (a) a cobalt carbonyl, (b) a hydrido cobalt carbonyl and (c) a cobalt-containing material convertible to a cobalt carbonyl or a hydrido cobalt carbonyl, an iodine promotor and a thiol defined by the formula:RSHwherein R is selected from the group consisting of saturated or unsaturated, straight or branched chain alkyl radicals having from one to 24 carbon atoms, cycloalkyl radicals having from three to 40 carbon atoms, aryl radicals having from six to 20 carbon atoms, aralkyl and alkaryl radicals having from six to 40 carbon atoms and halogen substituted derivatives thereof. A high degree of selectivity towards the formation of butanol and butanal is provided by using the cobalt entity and the thiol in a molar ratio in the range of about 2:1 to about 10:1, based on elemental cobalt and sulfur. The reaction is conducted at elevated temperature and pressure conditions for a time sufficient to convert methanol to n-butanol and n-butanal.
    • 包括正丁醇和正丁醛的C 4化合物通过甲醇,氢气和一氧化碳在钴催化剂存在下制备,所述钴催化剂选自(a)羰基钴,(b)羰基钴和 (c)可转化为羰基钴或羰基钴的钴的物质,碘促进剂和由下式定义的硫醇:其中R选自饱和或不饱和的直链或支链烷基 具有1至24个碳原子,具有3至40个碳原子的环烷基,具有6至20个碳原子的芳基,具有6至40个碳原子的芳烷基和烷芳基及其卤素取代的衍生物。 基于元素钴和硫,通过使用钴实体和硫醇以约2:1至约10:1的摩尔比来提供对形成丁醇和丁醛的高度选择性。 反应在升高的温度和压力条件下进行足以将甲醇转化为正丁醇和正丁醛的时间。